Removing inorganic contaminants
Scout intake sheet
Challenge description
Many biogenic waste streams and sidestreams contain inorganic components, such as chalk, minerals and/or heavy metals. There is a variety of ways in which these minerals and heavy metals can end up in waste streams and there is large heterogeneity within the type, amount, and size of these inorganic components. These contaminants can limit them in being used or processed to create additional value. The most common heavy metals are lead (Pb), nickel (Ni), chromium (Cr), cadmium (Cd), arsenic (As), mercury (Hg), zinc (Zn) and copper (Cu). For minerals, mainly clays, CaCO3, and NPK , Cl, Na compounds can be present in concentrations that are limiting further potential use-cases. Several members of the BCB platform are experiencing this issue as a hindrance to the valorization of their process streams and wastes. This scouting project will identify ways how to remove or separate these contaminants from sludge, slurries, and waste-water (semi-solid to liquid streams, >90% water).
Scope
Current known technique(s)
- Membrane technology
- Electrolysis
- Ab/Adsorption
- Treatment of the source
- Chemical removal
- Bioleaching
- Freeze concentration
- Gravitation
- Flotation
- Filtration
Ideal outcome
- Membrane technology
- Electrolysis
- Ab/Adsorption
- Treatment of the source
- Chemical removal
- Bioleaching
- Freeze concentration
- Gravitation
- Flotation
- Filtration
A simple and affordable solution to remove all unwanted heavy metals and/or minerals from (organic) waste streams; a solution that is applicable and was not known before.
Minimum viable outcome
An overview of removal technologies and their specifications.
Objective(s)
- Efficiency
- Cost
- Technology readiness level
- Input (biomass/contaminant)
- Selectivity
- Capacity
- high organic content
- Low inorganic content
- Scale of operation
Functions
Action = [remove] OR [separate] OR [fractionate] OR [reclaim]
Object = [heavy metal] OR [contaminant] OR [mineral] OR [inorganics]
Environment =
[slurry] OR [water] OR [sludge] OR [manure]
Terminology
- heavy metal
- contaminant
- mineral
- NPK
- CaCO3
- leaching
- waste stream
- slurry
- sludge
- manure
- aerobic biomass
- digestate
- Inert material
Preliminary Results
Published 06/10/2020
Based on the case described above we have executed the first line of queries in IGOR^AI. The goal was to obtain a broad set of techniques that Remove inorganic pollutants. 6 concepts are distinguished based on the results: 1. Physico-chemical 2. Sorption materials 3. Electro-treatment 4. Biological 5. Membrane technologies 6. Others Every concept comprises multiple techniques (43 in total). Below the table, short descriptions, research findings and sources per techniques are listed as well. You can use this information to get a better understanding of the techniques. During the midway meeting, we would like to discuss the techniques and concepts, determine their relevance and select the top selection that needs to be deepened in the second phase of the project.
To determine which technologies are relevant to proceed to the next scouting phase you can play the technology selection game by clicking on the button below.
1. Physico-chemical
BackProcesses such as extraction, precipitation and coaggulation using chemical means, or solvents.
1.1 Chemical removal
Acid treatment and chemical extracting agents can be used to remove heavy metals from wastewater and sludge:
**Highlights:**
* The concentration of heavy metals in excess sludge from municipal wastewater treatment plants has restricted its conversion to soil fertilizer, so it is necessary to remove the heavy metals from sludge. In this article, **the effects of heavy metal removal by some mineral acids such as HCl, H2SO4, H3PO4, HNO3 were analysed**, when treating excess sludge from a second sediment tank in municipal wastewater treatment plants. To improve the treatment, a combination of H2O2 and acid was also investigated. Aided by H2O2, the removal by the acid was enhanced. The suitable dosage of H2O2 was specially related to the solid content of sludge, pH and the acid kind.[ \[Art. #ARTNUM\]](#article-96099-2081073710)
* For chemical extraction, because of the adverse impacts that can result from the use of inorganic acids and complexing agents, interest can be directed more toward **utilizing organic acids as extracting agents** because of their biodegradability and capability to remove metals at mildly acidic condition, hence requiring less acid. [\[Art. #ARTNUM\]](#article-96099-2140127378)
* Demetalization of Pb, Ni, Zn, Cu and Cr heavy metal ions from sea sand and real samples of sewage sludge by subcritical water and supercritical carbon dioxide was investigated. **The best extraction efficiencies were obtained using acetyl acetonate as a chelating agent in both subcritical water** and supercritical CO2 extractions for real and artificial samples. The highest recoveries obtained from real samples for Cr, Cu, Ni, Pb and Zn were 77.25, 95.1, 84.82, 94.92 and 98.39 %, respectively, using the chelating agent in the subcritical water extraction.[\[Paper\]](https://www.researchgate.net/publication/261859713_Subcritical_and_supercritical_fluid_extraction_of_heavy_metals_from_sand_and_sewage_sludge)
| 1.1.1 | Chemical removal |
|---|---|
| Efficiency of Washing Techniques for Removal of Heavy Metals from Industrial Sludge | |
| The effluent treatment plant sludge is one of the major sources of contamination with toxic metals. Since the sludge contains heavy metals, it must be pretreated to reduce the contamination. The heavy metals from the sludge can be reduced/ separated by washing it with a suitable leaching solution. In the present study, the efficiencies of three leaching solutions to remove the contaminants from an industrial sludge were studied and the leaching process was modeled. The leaching solutions used are 0.1 N HCl, 0.1 N EDTA and 0.1 N FeCl3. The efficiencies of leaching solutions were assessed by conducting column leaching experiments on the sludge and the migration rates of heavy metal ions of Cu, Zn, Ni, Cd, Pb, Fe and Cr present in the sludge were estimated. These migration rates are useful to estimate the quantity of leaching solution required at the site to achieve the required levels of concentrations in the sludge. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
| 1.1.2 | Chemical removal |
| Heavy metal removal from contaminated sludge for land application : A review | |
| In recent years, various methods for heavy metal removal from sewage sludge have been extensively studied in order to minimize the prospective health risks of sludge during land application. In this paper, a comparative review and critical analysis of the application of chemical extraction, bioleaching, electroreclamation, and supercritical fluid extraction (SFE), in removing heavy metals from contaminated sludges is presented. Moreover, speciation studies, which can indicate ease of leachability of the different forms of heavy metals in sludge, are also presented. Experimental studies revealed a broad range in metal extraction efficiencies of the different extraction technologies. Acid treatment seemed to effectively remove Cd, attaining as much as 100% removal for some studies, as compared to bioleaching. SFE also gave higher removal efficiency than bioleaching. Cr, Pb and Ni seemed to be also effectively removed by the acid treatment. For the removal of Cu, Mn and Zn, the bioleaching process seemed to be appropriate with maximum removal efficiencies of 91%, 93% and 96% for the three metals, respectively, and as high as 64% minimum removal efficiency for Zn. The SFE process also gave good results for Cu, Mn and Zn removal. Electroreclamation exhibited better removal efficiency for Mn, but is still inferior to acid treatment and bioleaching processes. For chemical extraction, because of the adverse impacts that can result from the use of inorganic acids and complexing agents, interest can be directed more toward utilizing organic acids as extracting agents because of their biodegradability and capability to remove metals at mildly acidic condition, hence requiring less acid. The bioleaching process, although it seems to give a higher yield of metal extraction with lower chemical cost than chemical extraction, may be limited by the inability of the system to cope with the natural environmental conditions, requires strict monitoring of aeration rate and temperature and has applicability to only low sludge solids concentration. A full-scale study would be useful to better assess the efficiency of the process. The electroreclamation technology is limited by its relatively higher energy consumption and limited applicability to sludge. The SFE method, on the other hand, is limited by the complexity of the process and the cost of ligands suitable for effective metal extraction. Both of these technologies are still in their early stage of application and hence there is a need for further basic and applied studies. Finally, the common advantage for almost all treatment technologies studied is that the extraction efficiencies for some metals are high enough to remove metals from sludge to levels suitable for land application. | |
| 01/01/2006 00:00:00 | |
| Link to Article | |
| 1.1.3 | Chemical removal |
| Recycling of sludge with the Aqua Reci process. | |
| Supercritical Water Oxidation (SCWO) is an innovative and effective destruction method for organics in sewage sludge. The SCWO process leaves a slurry of inorganic ash in a pure water phase free from organic contaminants, which opens possibilities for a simple process to recover components like phosphates and/or coagulants from the sewage sludge, a process marketed as the Aqua Reci. In a continuous pilot plant for the SCWO process digested sludge has been treated. The ash has been extracted in lab- and pilot scale with both caustic and acids in order to recover phosphates and coagulants. The particle size of the inorganic contaminants in the water after the SCWO process is between 1-10 μm, which means that it is very reactive. The phosphate, and partly the aluminium, can be extracted with caustic as iron and heavy metals are completely insoluble in caustic. This is a method to separate the phosphates from the rest of the contaminants. However, high calcium content will bind the phosphate as calcium phosphate insoluble in caustic. In most cases the calcium content is too high and the best solution is to dissolve phosphates and all metals with sulphuric acid. From this solution first iron phosphate can be separated and thereafter in a second step aluminium and finally heavy metals in a third step. Iron can be separated from the phosphate, either by leaching the phosphate with caustic off to sodium phosphate leaving a precipitate consisting of iron hydroxide, or the iron phosphate can be dissolved in hydrochloric acid followed by a liquid extraction process where ferric chloride can be separated leaving a phosphoric acid. By the acid dissolving process it is possible to recover phosphate, iron, aluminium, and heavy metals from the inorganic since the Aqua Reci process only leaves a silica residue representing about 10% of the DS content in the original sludge. | |
| 05/01/2004 00:00:00 | |
| Link to Article | |
| 1.1.4 | Chemical removal |
| Treatment of Excess Sludge Containing Heavy Metal by Chemical Ways | |
| The concentration of heavy metals in excess sludge from municipal wastewater treatment plants has restricted its convertion to soil fertilizer, so it is necessary to remove the heavy metals from sludge. In this article, the effects of heavy metal removal by some mineral acids such as HCl, H2SO4, H3PO4, HNO3 were analysed, when treating excess sludge from a second sediment tank in municipal wastewater treatment plants. To improve the treatment, a combination of H2O2 and acid was also investigated. Consequently, the difference of heavy metal removal among those acids was showed. Its removal of Hg by HNO3 was better than by other acids. Lower pH enhanced the dissolving of heavy metal, yet the removal of Cr was insensitive to the pH. Aided by H2O2, the removal by the acid was enhanced. The suitable dosage of H2O2 was specially related to the solid content of sludge, pH and the acid kind. | |
| 05/01/2012 00:00:00 | |
| Link to Article | |
| 1.1.5 | Chemical removal |
| Treatment of slaughterhouse wastewater by acid precipitation (H2SO4, HCl and HNO3) and oxidation (Ca(ClO)₂, H2O2 and CaO₂) | |
| Abstract The treatment of slaughterhouse wastewater was investigated by both acid precipitations and by oxidation processes. Precipitation tests were developed using three acids (H2SO4, HCl and HNO3) at different operating pH (1–6). A decrease of the precipitation pH led to an increase of the conductivity values of the supernatant. Precipitation processes allowed the removal of chemical oxygen demand (COD) (41–97%), turbidity (56–99%) and total phosphorus (27–56%). Total phenols were removed (15–96%) from pH ≥ 2, depending on the precipitation process. Generally, precipitation processes decreased the hydroxide and bicarbonates species. Additionally, three different oxidation processes were tested at different concentrations (1–15 g L−1): Ca(ClO)₂, H2O2 and CaO₂. When Ca(ClO)₂ and CaO₂ were applied, an increase of the supernatant conductivity was achieved. COD removal ≥71% and turbidity elimination in the range of 85–100% were achieved by using oxidation processes. CaO₂ was very effective to remove total phosphorus (81–96%). The increase of the oxidant concentration in H2O2 and Ca(ClO)₂ oxidation processes led to a decrease in the removal of total phenols and bicarbonates species. Optical density of the microorganism cultures was efficiently eliminated (up to 100%) by oxidation processes. In addition, acid precipitation and oxidation allowed to remove total solids (TS), total volatile solids (TVS), total suspended solids (TSS), ammonia nitrogen, nitrates and biochemical oxygen demand (BOD5). Acid precipitation and oxidation produced sludge rich in organic matter and nutrients (Ca, Mg, P, Cl, Na and K). Despite the high removal efficiencies, a post-treatment following the precipitation and oxidation processes can be required. | |
| 11/01/2019 00:00:00 | |
| Link to Article | |
1.2 Supercritical fluid extraction (SFE)
Supercritical fluid extraction is the process of separating one component from another using supercritical fluids as the extracting solvent. Extraction is usually from a solid matrix, but can also be from liquids.[\[Wiki\]](https://en.wikipedia.org/wiki/Supercritical_fluid_extraction)
**Highlights:**
* SFE also gave higher Cr removal efficiency than bioleaching. The SFE process also gave good results for Cu, Mn and Zn removal. the SFE method, on the other hand, is limited by the complexity of the process and the cost of ligands suitable for effective metal extraction. [\[Art. #ARTNUM\]](#article-96103-2140127378)
* Demetalization of Pb, Ni, Zn, Cu and Cr heavy metal ions from sea sand and real samples of sewage sludge by subcritical water and **supercritical carbon dioxide** was investigated. Experimental parameters such as temperature, pressure, extraction time in the static and dynamic mode and sampling were optimized in order to determine the suitable conditions for high removal of metals. The best extraction efficiencies were obtained using acetyl acetonate as a chelating agent in both subcritical water and supercritical CO2 extractions for real and artificial samples. Samples collected from extraction system using both subcritical water and supercritical carbon dioxide were analyzed by inductively coupled plasma mass spectrometry (ICP-MS). The highest recoveries obtained from real samples for Cr, Cu, Ni, Pb and Zn were 77.25, 95.1, 84.82, 94.92 and 98.39 %, respectively, using the chelating agent in the subcritical water extraction.[\[Paper\]](https://www.researchgate.net/publication/261859713_Subcritical_and_supercritical_fluid_extraction_of_heavy_metals_from_sand_and_sewage_sludge)
| 1.2.1 | Supercritical fluid extraction (SFE) |
|---|---|
| A Review for Heavy Metal Removal from Sludge | |
| Removing the total amount of heavy metals efficiently from sludge was the key of its land application. In this paper, a review of chemical extraction, bioleaching, electro reclamation, and supercritical fluid extraction (SFE) in removing heavy metals from sewage sludge is presented in aspect of principle, research actuality and application. Moreover, the efficiencies, advantages and disadvantages of these methods are compared in order to offer theories to innocent and utilization of the sewage sludge. | |
| 01/01/2007 00:00:00 | |
| Link to Article | |
| 1.2.2 | Supercritical fluid extraction (SFE) |
| Heavy metal removal from contaminated sludge for land application : A review | |
| In recent years, various methods for heavy metal removal from sewage sludge have been extensively studied in order to minimize the prospective health risks of sludge during land application. In this paper, a comparative review and critical analysis of the application of chemical extraction, bioleaching, electroreclamation, and supercritical fluid extraction (SFE), in removing heavy metals from contaminated sludges is presented. Moreover, speciation studies, which can indicate ease of leachability of the different forms of heavy metals in sludge, are also presented. Experimental studies revealed a broad range in metal extraction efficiencies of the different extraction technologies. Acid treatment seemed to effectively remove Cd, attaining as much as 100% removal for some studies, as compared to bioleaching. SFE also gave higher removal efficiency than bioleaching. Cr, Pb and Ni seemed to be also effectively removed by the acid treatment. For the removal of Cu, Mn and Zn, the bioleaching process seemed to be appropriate with maximum removal efficiencies of 91%, 93% and 96% for the three metals, respectively, and as high as 64% minimum removal efficiency for Zn. The SFE process also gave good results for Cu, Mn and Zn removal. Electroreclamation exhibited better removal efficiency for Mn, but is still inferior to acid treatment and bioleaching processes. For chemical extraction, because of the adverse impacts that can result from the use of inorganic acids and complexing agents, interest can be directed more toward utilizing organic acids as extracting agents because of their biodegradability and capability to remove metals at mildly acidic condition, hence requiring less acid. The bioleaching process, although it seems to give a higher yield of metal extraction with lower chemical cost than chemical extraction, may be limited by the inability of the system to cope with the natural environmental conditions, requires strict monitoring of aeration rate and temperature and has applicability to only low sludge solids concentration. A full-scale study would be useful to better assess the efficiency of the process. The electroreclamation technology is limited by its relatively higher energy consumption and limited applicability to sludge. The SFE method, on the other hand, is limited by the complexity of the process and the cost of ligands suitable for effective metal extraction. Both of these technologies are still in their early stage of application and hence there is a need for further basic and applied studies. Finally, the common advantage for almost all treatment technologies studied is that the extraction efficiencies for some metals are high enough to remove metals from sludge to levels suitable for land application. | |
| 01/01/2006 00:00:00 | |
| Link to Article | |
1.3 Chemical precipitation
Precipitation using a precipitation agent (usually in the form of hydroxide/ lime) is a common separation technique, which can both remove heavy metals and phosphorus compounds.
Other (inorganic) chemical precipitants have also been used, such as alum (for phosphorus removal) and ferric salts (FeCl3).
**Highlights:**
* Chemical precipitation is the most widely used for heavy metal removal from inorganic effluent. Adjustment of pH to the basic conditions (pH 9–11) is the major parameter that significantly improves heavy metal removal by chemical precipitation. **Lime and limestone are the most commonly employed precipitant agents due to their availability and low-cost in most countries.** [\[Paper\]](https://www.sciencedirect.com/science/article/pii/S1878535210001334#:\~:text=2.3.&text=The%20conventional%20processes%20for%20removing,metal%20removal%20from%20inorganic%20effluent.)
* Presently, phosphorus is traditionally removed from wastewater using chemical precipitation or biological methods, ending up in unusable products or excess sludge. **Chemical (nonmetallic) precipitation, under controlled condition, could constitute a sustainable approach for achieving this goal, with the formation of struvite (magnesium ammonium phosphate hexahydrate) or other calcium phosphate compounds**, which have great potential of being used as fertilizers. In this study, experimental and pilot-test conditions for recovery of P-based fertilizers from aerobically treated sludge are analyzed, estimating at the same time the economic and energy consequences of several process approaches on the treatment facility operation. [\[Art. #ARTNUM\]](#article-96072-2920892624)
* The reduction of sulfate ions from the industrial wastewater using advanced **calcium-aluminum precipitation** method (ACAPM) has been evaluated. The ACAPM involved the precipitation of sulfate ions as minerals like gypsum and ettringite via calcium/ aluminum compounds. Experimental results indicate that the ACAPM was effectively reduced sulfate with removal efficiency exceed 98%. It also effectively removed heavy metals including: Cr, Ni, Cd, Pb, Fe, Mn & Zn, with removal efficiencies up to 99%. Results showed that the ACAPM has remarkable sulfate ions removal efficiency with high concentrations.[ \[Art. #ARTNUM\]](#article-96072-2989754776)
* Phosphorus removal is an important issue in the field of water and wastewater treatment. In this study, a starch-based flocculant (St-CTA), as an assisting agent, was fed after the application of traditional inorganic precipitant of **ferric chloride (FeCl3) to remove inorganic and organic phosphorus** from their respective simulated turbid wastewaters.[ \[Art. #ARTNUM\]](#article-96072-2991298135)
* Wastewater samples from battery, paint and textile industries were treated with different doses of locally **available alum, aluminum sulphate and ferric chloride** in order to determine and compare their effectiveness in removing heavy metal contents from the wastewaters.[ \[Art. #ARTNUM\]](#article-96072-2008496022)
| 1.3.1 | Chemical precipitation |
|---|---|
| Biosorption of Heavy Metal by Algae Biomass in Surface Water | |
| Discharging wastewater containing heavy metals of Cu, Pb, Zn and Cd into water bodies can cause toxicity in plants and aquatic animals and some of them will be unable to survive except algae. Wastewater treatment method to remove heavy metal contaminants includes chemical precipitation, ion exchange, membrane, filtration, adsorption using activated carbon. However, these methods are either expensive or have other disadvantages such as high energy consumption and inefficiencies when existing heavy metals are at trace concentration. Biosorption using algae biomass can be an alternative method to eliminate heavy metals. The objective of the project is to investigate the capability of Marine Algae (MA) and Freshwater Algae (FA) bi-omass in adsorbing heavy metals of Cu, Pb, Zn and Cd from water medium using synthetic water and industrial water. MA and FA were obtained from the eastern coast of Pulau Ubin and local fish farm respectively. After being fully washed with deionised water, dried in a furnace for 105°C, they are grinded to pass 1 mm2 of siever. MA and FA were characterised using FTIR to determine their functional groups. An industrial water was collected from industrial discharge from metal fac-tories in northern side of Singapore. Effect of adsorption time, adsorbent concentra-tion, and pH were studied. The result showed that FA and MA had a higher capability in adsorbing a total metal of about 40 ppm level from an industrial water, or 4 times than synthetic water concentration, at the same adsorbent dosage of 50 mg. In con-clusion, the presence of various functional groups, hydroxyl, carboxylic and amine groups, in all MA and FA samples had enabled the algae biomass to adsorb heavy metals of Cu, Pb, Cd and Zn from synthetic and industrial water. Due to their bio-sorptive properties and fast adsorption capability, algae could be a potential method for cleaning up surface water or post-treatment of wastewater and minimise the cost of eutrophication. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 1.3.2 | Chemical precipitation |
| Economic and energetic assessment of different phosphorus recovery options from aerobic sludge | |
| Abstract Phosphorus removal from Wastewater Treatment Plant effluents is mandated by law under many circumstances, at the same time, the need for more efficient P recovery technologies in the form of valuable reusable products is also increasing, with the aim of conciliating environmental quality as well as the element’s scarcity concerns. Several researchers have identified municipal wastewater as one of the most promising sources of phosphorus recovery, as other recovery pathways are often limited by leaks and short-circuits in the P anthropic cycle. Presently, phosphorus is traditionally removed from wastewater using chemical precipitation or biological methods, ending up in unusable products or excess sludge. Chemical (nonmetallic) precipitation, under controlled condition, could constitute a sustainable approach for achieving this goal, with the formation of struvite (magnesium ammonium phosphate hexahydrate) or other calcium phosphate compounds, which have great potential of being used as fertilizers. In this study, experimental and pilot-test conditions for recovery of P-based fertilizers from aerobically treated sludge are analyzed, estimating at the same time the economic and energy consequences of several process approaches on the treatment facility operation. | |
| 03/01/2019 00:00:00 | |
| Link to Article | |
| 1.3.3 | Chemical precipitation |
| Effective phosphorus removal by adding alum to septic tank | |
| Phosphorus is considered a key element in causing excessive water fertilization which in turn brings about an abundant growth of algae and other aquatic plants leading to deteriora tion of water quality. Vollenweiderx and Thomas2 demonstrate numerous examples of eutrophication of lakes in North America and Europe caused by phosphorus entering the lakes from different sources. Human activity, especially inadequately treated human waste water, is one of the sources. Kolenbrander 3 showed that 38 percent of the total accumu lation of phosphorus in fresh surface waters in The Netherlands comes from release of un purified wastewater. The average amount of phosphorus con tained in domestic wastewater is about 0.8 kg/ person year.1 Most of the phosphorus found in excreta and urine is in a form of orthophos phates. Phosphorus occurs in cleaning agents in the form of polyphosphates (tripolyphos phates or pyrophosphates) but is hydrolysed fairly quickly to orthophosphate in wastewater. In many countries there are no standards or regulations limiting the permissible level of phosphorus concentration in effluent before dis charging it into ground or surface waters. The wastewater treatment plants in the U. S. and Canada have adopted a permissible concentra tion for the Great Lakes of 1.0 mg/1 (as P) in accordance with the recommendations of the 1972 Canada-United States Agreement on Great Lakes Water Quality.4 The Swedish law governing environmental protection limits P concentration to about 0.5 mg/1 (as P).5 It has been observed that when subsurface disposal systems are built on proper soil con taining sufficient quantities of fine grain par ticles like clay and silt, and when the systems are located at proper distances from the re ceiving water body, the removal of the phos phorus from the septic tank effluent by the soil is almost complete.6 However, when the dis tances between the disposal system to the lake are limited or in cases when only coarse sand or even bare bedrock are the media separating the disposal system from the water, the phos phorus from the system moves directly into the groundwater or into the lake or river. In such situations it is desirable to remove the phos phorus from the wastewater before the septic tank effluent leaves the tank. The purpose of this study was to develop a simple and economical method for separating the phosphorus and other contaminants from the wastewater inside the septic tank. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 1.3.4 | Chemical precipitation |
| Efficient removal of phosphorus from turbid water using chemical sedimentation by FeCl3 in conjunction with a starch-based flocculant | |
| Abstract Phosphorus removal is an important issue in the field of water and wastewater treatment. In this study, a starch-based flocculant (St-CTA), as an assisting agent, was fed after the application of traditional inorganic precipitant of ferric chloride (FeCl3) to remove inorganic and organic phosphorus from their respective simulated turbid wastewaters. The effects of various influencing factors, including CTA content of St-CTA, dosage, initial pH, initial turbidity, and initial total phosphorus (TP), were investigated systematically. This modified chemical sedimentation process assisted by St-CTA not only showed high efficient in removing TP and turbidity but also evidently reduced the required dosage of FeCl3. This combination exhibited better efficiency in removing organic TP than in removing inorganic TP from water. The synergistic mechanisms of FeCl3 and St-CTA were discussed in detail by combination of apparent removal effects and floc properties. St-CTA exhibits strong charge neutralization and bridging flocculation effects and can thus efficiently aggregate and precipitate various phosphorus and iron complexes previously formed through chemical sedimentation, adsorption, and chelation. Besides, the validation of this combination usage was further confirmed by treating a real wastewater, and half of the required FeCl3 dosage and one third of the total cost were saved after addition of only 0.4 mg/L St-CTA when 90% TP and 95% turbidity were reduced. This study thus provided a novel technique for the diminution of TP and turbidity in turbid wastewater, considerable reduction of FeCl3 dosage and final cost, and lowering of secondary pollution risk. | |
| 03/01/2020 00:00:00 | |
| Link to Article | |
| 1.3.5 | Chemical precipitation |
| Precipitation of iron-hydroxy-phosphate of added ferric iron from domestic wastewater by an alternating aerobic-anoxic process | |
| Abstract Removal of phosphorus from a municipal wastewater by simultaneous precipitation of iron-hydroxy-phosphate (IHP) was investigated. The addition of Fe 3+ was performed to supplement biological excess phosphorus removal by a completely mixed alternating aerobic–anoxic (AAA) activated sludge process. The cycles of 3-h anoxic time and 3-h aerobic digestion were set to controlling a single-sludge nitrification–denitrification. In this study, attempt has been made to analyse the effects of initial dissolved Fe/P molar ratio and pH on IHP precipitation. The AAA treatment process to remove soluble reactive and total phosphorus from domestic wastewater had a moderate efficiency. The empirical formula of IHP that differs from different pH ranges was verified. Two types of Fe 4 (OH) 9 PO 4 and Fe 5 (OH) 6 (PO 4 ) 3 precipitate may occur in different conditions of the AAA process. The efficiency of phosphorus removal from domestic wastewater by an AAA process was verified to contribute to a working methodology for the application of technologies in the field of domestic wastewater treatment. | |
| 10/01/2014 00:00:00 | |
| Link to Article | |
| 1.3.6 | Chemical precipitation |
| Removal Of Heavy Metals From Industrial Wastewaters Using Local Alum And Other Conventional Coagulants - a comparative study | |
| Wastewater samples from battery, paint and textile industries were treated with different doses of locally available alum, aluminum sulphate and ferric chloride in order to determine and compare their effectiveness in removing heavy metal contents from the wastewaters. The percentage removal of the metals from the industrial wastewaters increased with mgL-l dosage of the coagulants used with optimal performance generally at a slightly alkaline pH. Local alum proved to be equally effective in removing heavy metals from the industrial wastewater samples compared with the conventional aluminium sulphate and ferric chloride. IFE Journal of Science Vol. 9 (2) 2007 pp. 185-190 | |
| 10/01/2007 00:00:00 | |
| Link to Article | |
| 1.3.7 | Chemical precipitation |
| Soil Treatment System Using Nanobubble and Multi-Stage Washing of Inorganic Acid | |
| The present invention advances the fuel decomposition and heavy metals desorbed using nano bubbles and a quantitative supply, a composite soil contaminated with oil contaminants and heavy metals by the heavy metals act through the multi-stage washing of the inorganic acid to provide the removal of the heavy metals more efficiently and a plurality of feed conveyors, the transfer is disposed between the feeding conveyor which is configured to include a contaminated soil separator to proceed with the one magnetic separation and particle size selection accommodate contaminated soil sequentially selecting unit; In the first washing tank, washing is possible to accommodate the contaminated soil selected from the feeding selection unit, it is provided one end connected to the first washing tank to Flotation the oil contaminants and heavy metals adsorbed by the contaminated soil towards the first washing tank single-stage washing unit consisting of a first bubble generator injecting nanobubbles and; And a second washing tank to re-washable to accommodate the contaminated soil via the first-stage washing section, is provided connected to one of said second washing tank to Flotation the oil contaminants and heavy metals adsorbed by the contaminated soil towards said second washing tank a two-stage washing unit consisting of a second bubble generator of injecting nanobubbles and; It can be respectively connected to the first-stage washing section a first washing tank and a second washing tank the two-stage washing section, and removing the heavy metals in the soil contaminated by leaching action of mineral acids for each inorganic acids towards the first washing tank and the second washing tank It provides compound contaminated soil purifying system using a multi-stage washing nanobubbles and inorganic acids containing; injection unit for injecting an inorganic acid. | |
| 07/08/2016 00:00:00 | |
| Link to Article | |
| 1.3.8 | Chemical precipitation |
| Sulfate Reduction and Heavy Metals Removal from Industrial Wastewater via Advanced Calcium-Aluminum Precipitation Method | |
| The reduction of sulfate ions from the industrial wastewater using advanced calcium-aluminum precipitation method (ACAPM) has been evaluated. The ACAPM involved the precipitation of sulfate ions as minerals like gypsum and ettringite via calcium/ aluminum compounds. Factors affecting the reduction of sulfate ions such as: pH, Ca(OH)2 and NaAlO2 dosages have been investigated, while the optimal experimental conditions for sulfate ions reduction were determined. The precipitated solids have been characterized by X-ray diffraction (XRD), scanning electron microscope (SEM), and energy dispersive spectroscopy (EDS), respectively. Experimental results indicate that the ACAPM was effectively reduced sulfate with removal efficiency exceed 98%. It also effectively removed heavy metals including: Cr, Ni, Cd, Pb, Fe, Mn & Zn, with removal efficiencies up to 99%. Results showed that the ACAPM has remarkable sulfate ions removal efficiency with high concentrations. | |
| 11/11/2019 00:00:00 | |
| Link to Article | |
| 1.3.9 | Chemical precipitation |
| Treatment of slaughterhouse wastewater by acid precipitation (H2SO4, HCl and HNO3) and oxidation (Ca(ClO)₂, H2O2 and CaO₂) | |
| Abstract The treatment of slaughterhouse wastewater was investigated by both acid precipitations and by oxidation processes. Precipitation tests were developed using three acids (H2SO4, HCl and HNO3) at different operating pH (1–6). A decrease of the precipitation pH led to an increase of the conductivity values of the supernatant. Precipitation processes allowed the removal of chemical oxygen demand (COD) (41–97%), turbidity (56–99%) and total phosphorus (27–56%). Total phenols were removed (15–96%) from pH ≥ 2, depending on the precipitation process. Generally, precipitation processes decreased the hydroxide and bicarbonates species. Additionally, three different oxidation processes were tested at different concentrations (1–15 g L−1): Ca(ClO)₂, H2O2 and CaO₂. When Ca(ClO)₂ and CaO₂ were applied, an increase of the supernatant conductivity was achieved. COD removal ≥71% and turbidity elimination in the range of 85–100% were achieved by using oxidation processes. CaO₂ was very effective to remove total phosphorus (81–96%). The increase of the oxidant concentration in H2O2 and Ca(ClO)₂ oxidation processes led to a decrease in the removal of total phenols and bicarbonates species. Optical density of the microorganism cultures was efficiently eliminated (up to 100%) by oxidation processes. In addition, acid precipitation and oxidation allowed to remove total solids (TS), total volatile solids (TVS), total suspended solids (TSS), ammonia nitrogen, nitrates and biochemical oxygen demand (BOD5). Acid precipitation and oxidation produced sludge rich in organic matter and nutrients (Ca, Mg, P, Cl, Na and K). Despite the high removal efficiencies, a post-treatment following the precipitation and oxidation processes can be required. | |
| 11/01/2019 00:00:00 | |
| Link to Article | |
| 1.3.10 | Chemical precipitation |
| Treatment of swine wastewater combined with MgO-saponification wastewater by struvite precipitation technology | |
| Abstract The total ammonia nitrogen (TAN) was removed from swine wastewater using MgO-saponification wastewater as the source of magnesium for struvite precipitation. The experimental results indicated that pH regulators had a significant effect on the extent of struvite precipitation. The effect of pH regulators on the TAN removal ratio was as follows: K 2 CO 3 > KOH > Na 2 CO 3 > NaOH at identical pHs. The corresponding order for the removal of phosphate was KOH > NaOH > K 2 CO 3 > Na 2 CO 3 . When struvite crystallization occurred in the presence of ferric ions at 0–500 mg/L concentration, the TAN removal ratio decreased from 89.7% to 82%. Nevertheless, the removal ratio could be remarkably improved by intermittent addition of magnesium source. The pilot-scale experiments revealed that an average of 93% (±3%) TAN removal could be achieved in a continuous-flow reactor by dosing the MgO-saponification wastewater at Mg:N:P ratio of 1.1:1:1 via seeding crystal technique. An economic evaluation showed that the cost for struvite precipitation could be reduced by approximately 12.4% using the combined treatment of swine wastewater and MgO-saponification wastewater as compared with the use of pure magnesium salts. | |
| 10/01/2014 00:00:00 | |
| Link to Article | |
1.4 Sulfide precipitation
Sulfide precipitation uses a sulfide precipitant, such as Na2S, NaHS and H2S to precipitate heavy metals, which generally results in a more complete removal than using OH.
**Highlights:**
* **Sulfide as a product of dissimilatory sulphate reduction may remove heavy metals from wastewaters via the precipitation of metal sulphide and the use of CWs in treating heavy metal containing waters (e.g. acid mine drainage) is increasing.** [ \[Art. #ARTNUM\]](#article-96097-2052401730)
* Sulfide precipitation of heavy metal containing wastewaters results in low effluent concentrations. However, sulphide precipitation is not widely applied in practice because the dosing of sulphide cannot adequately be controlled. **A new process was developed where the combination of a sulphide-selective electrode (pS-electrode) and pH electrode controls the sulphide addition. The metals were removed to levels <0.05 mg.l^-1^ at pH 6.0 by sulphide precipitation while maintaining a total sulphide concentration <0.02 mg.l^-1^.** [\[Paper\]](https://iwaponline.com/wst/article/47/10/9/10266/Innovative-developments-in-the-selective-removal)
| 1.4.1 | Sulfide precipitation |
|---|---|
| Sulphur transformations in constructed wetlands for wastewater treatment: A review | |
| Abstract The sulphur-cycle processes inside constructed wetlands (CWs) and their role in the complex network of transformation processes and the long-term stability of wetland systems are still not sufficiently understood. A comprehensive review is accordingly necessary for better understanding to optimize the future design and operation of wetland systems. In this paper, the concept of sulphur cycling in CWs in principle, transformations dynamics of sulphur compounds and their interactions with other element cycles (such as carbon, nitrogen and phosphorus) and plants, as well as importance for treatment efficiencies are reviewed. The abiotic and biotic transformations of sulphur are both spatially and temporally dynamic in CWs. Next to physico-chemical processes, e.g. mineral precipitation and dissolution, biologically catalyzed redox reactions such as assimilatory and dissimilatory sulphate reduction, as well as oxidation/reduction, and disproportionation of more reduced sulphur compounds also simultaneously occur in the rooted zones of CWs. Moreover, the interactions between sulphur transformations and other processes including microbial transformations of carbon, nitrogen and phosphorus, as well as the impact of plants are discussed. Briefly, sulphide as a product of dissimilatory sulphate reduction may remove heavy metals from wastewaters via the precipitation of metal sulphide and the use of CWs in treating heavy metal containing waters (e.g. acid mine drainage) is increasing. However, high sulphide concentrations may also negatively affect growth of wetland plants and microbial activities, especially nitrification, but also influence the mobilization of iron-bound phosphorus. This information may be used to offer future design and operational methodologies that might enhance the performance of contaminants removal and drive a sustainable management of CWs for wastewater treatment. | |
| 03/01/2013 00:00:00 | |
| Link to Article | |
1.5 Ferrite process
Ferrite (Fe~3~O~4~), a magnetic iron oxide containing Fe^2+^ and Fe^3+^ in the structure, has spinel structure and can be synthesized through the reaction depicted by Eq: 3Fe^2+^ + 6OH^−^ + 1/2O~2~ → Fe~3~O~4~ + 3H~2~O
When heavy metal ions coexist with Fe^2+^, they can be incorporated into the structure through co-precipitation. The principle of FP to treat heavy metals is presented in Eq.: *x*M^2+^ + (3 − *x*)Fe^2+^+ 6OH^−^ + 1/2O~2~ → M\*~x~\*Fe~(3−\*x\*)~O~4~ + 3H~2~O
**Highlights:**
* Complete removal of heavy metal from complex heavy-metal wastewater (CHMW) requires advanced technology. **This study investigated the feasibility of a multi-staged ferrite process (MSFP) for treating CHMW, containing Cd, Cu, Pb, Cr, Zn, Ag, Hg, Ni, Sn and Mn.** After the three-staged procedures, all heavy metals in supernatant and sludge could fulfill the contamination levels regulated by law. [ \[Art. #ARTNUM\]](#article-96100-2048778130)
* **The ferrite process (FP), which is another effective approach of treating metal ion-containing wastewater, can crystallize metal ions into ferrites; the sludge easily precipitates, is stable and can be recycled.** [\[Paper\]](https://link.springer.com/article/10.1007/s10661-008-0266-x)
| 1.5.1 | Ferrite process |
|---|---|
| Treatment of complex heavy metal wastewater using a multi-staged ferrite process | |
| Abstract Complete removal of heavy metal from complex heavy-metal wastewater (CHMW) requires advanced technology. This study investigated the feasibility of a multi-staged ferrite process (MSFP) for treating CHMW, containing Cd, Cu, Pb, Cr, Zn, Ag, Hg, Ni, Sn and Mn. Our experimental results showed that most of the supernatants after conventional single-step ferrite process could conform to the effluent standard of Environmental Protection Administration in Taiwan. However, the sludge could not satisfy the toxicity characteristic leaching procedure (TCLP) limits due to high Cd, Cu, and Pb concentrations. The performance of MSFP in removing heavy metals from wastewater was subsequently investigated and the parameters of three treating steps in MSFP were optimized under 70 °C and 90 °C at pH 9, and 80 °C at pH 10. After the three-staged procedures, all heavy metals in supernatant and sludge could fulfill the contamination levels regulated by law. In addition, the sludge generated from the MSFP was examined by XRD and forms a stable spinel structure, which could be effectively separated by external magnetic field. | |
| 03/01/2012 00:00:00 | |
| Link to Article | |
1.6 Coagulation–flocculation
In water treatment, coagulation flocculation involves the addition of compounds that promote the clumping of fines into larger floc so that they can be more easily separated from the water. Coagulation is a chemical process that involves neutralization of charge whereas flocculation is a physical process and does not involve neutralization of charge.[\[Wiki\]](https://en.wikipedia.org/wiki/Coagulation_(water_treatment))
**Highlights:**
* Coagulation–flocculation process is regarded as one of the most important and widely used treatment processes of industrial wastewaters due to its simplicity and effectiveness. This paper provides a critical review on recent studies of coagulation–flocculation treatment processes of various industrial wastewaters. The limitations and challenges for the coagulation–flocculation process such as the toxicity and health hazard posed by inorganic coagulants, production of large amount of toxic sludge, ineffectiveness in removing heavy metals and emerging contaminants, increase in effluent color, inefficient pollutant removal using natural coagulants, and complexity of scaling up procedure are presented. In addition, an overview on the influence of process parameters on treatment efficiency is included in this revie...[ \[Art. #ARTNUM\]](#article-96092-2333262005)
* Hematite wastewater containing dissolved heavy metals is a potential threat to eco-environment and human health. Flocculation as an efficient and cost effective water treatment technology should be applied in its treatment. A sulfonated chitosan-based flocculant (CS-g-P(AM-AMPS)) was prepared via graft copolymerization. **Dissolved heavy metals in the wastewater were removed by the chelation of sulfonate group in CS-g-P(AM-AMPS), the adsorption of other functional groups and the co-settlement with flocs.** [ \[Art. #ARTNUM\]](#article-96092-2979282107)
* In a previous work, a novel effluent treatment process was developed and applied to remove heavy metal ions from dilute aqueous solutions using polymer–surfactant aggregates (PSAs) (Shen et al., 2015). A subsequent pH adjustment method for the polymer–surfactant aggregate process has been developed to recover the heavy metal ions from the flocculated PSAs into a concentrated solution and to regenerate the PSAs for recycle. The PSA is a colloidal structure that is formed by micelle-like aggregates associating with the oppositely charged polymer chains. The PSA can then bind with heavy metal ions and precipitate out of the solution. In the work presented, the flocs are firstly acidified using a small volume of 0.05 M H 2 SO 4 . The bound metal ion are leached out in 15 min, and pass through a coarse filter to report as a metallic ions solution 20–50 times more concentrated than the original effluent. After the acid leaching, the flocs can be completely dissolved in a small volume of 0.1 M NaOH. This basic polymer and surfactant solution is then reused in the next treatment cycle; meanwhile, the pH of the solution is neutralised by adding H 2 SO 4 . The results show that the removal efficiency of 11.2 ppm Cd(II) solution remains above 97% after 5 cycles without the need for make-up of the removal agent. The recovery efficiencies of Cd(II), Zn(II), and Cr(III) remain above 91%, 86% and 73%, respectively, after 6 cycles. In addition, a MATLAB simulation shows that the accumulations of Na 2 SO 4 are stabilised at 280 ppm after the third cycle. Thus, the pH adjustment method is able to recover and concentrate the metal ions from the flocculated PSAs, and also to regenerate the removal agent such that it can be recycled with little deterioration of removal ability. [\[Art. #ARTNUM\]](#article-96092-2214003663)
| 1.6.1 | Coagulation–flocculation |
|---|---|
| A Study on the Particle Separation Technology of Contaminated Dredged Sediments | |
| As sediment contamination problems have recently been raised in Korea, the need for technologies to remove contaminants in sediments has increased. Contaminated sediments in Korea has been annually dredged and treated using processes of coagulation/flocculation, sedimentation on barges, dewatered and dried at prepared site, and then disposed at a landfill site, which is very costly, and only a limited landfill space available in Korea. Contaminants in media containing a high percentage of silt and clay sized particles, typically, are strongly adsorbed on the particles and difficult to remove. Particle separation processes that separate the fine clay and silt particles from the coarser sand and gravel and concentrate the contaminants into a smaller volume of sediment that can be further treated of disposed of, are very effective in the post step processes. In this study are to test the feasibility of treating dredged sediments using a hydrocyclone process, and to estimate design parameters for a pilot scale test. A hydrocyclone was operated to separate larger particles from the sediments. It was found that the particle separation was greatly affected by the solid contents and inlet pressure in the hydrocyclone. | |
| 09/30/2013 00:00:00 | |
| Link to Article | |
| 1.6.2 | Coagulation–flocculation |
| Characteristics and mechanisms of phosphorus removal by dewatered water treatment sludges and the recovery | |
| The use of novel industrial by-products (IBPs) to remove phosphorus (P), instead of high-cost P removal techniques, is one of the sustainable solutions to protect aquatic life from excessive P discharges. One of such IBPs is dewatered drinking water treatment works sludges generating from using aluminium or iron salts as coagulant during the drinking water treatment process. Previous studies have shown that the sludges hold promise as a novel adsorbent for the removal of P from wastewaters; however, comprehensive investigation into factors affecting the P removal and the recovery is lacking. Therefore, the main aim of this study is to contribute to a mechanistic understanding of P removal and retention by dewatered water treatment sludge (DWTS), and the associated coagulant recycling and P recovery from the P-saturated sludge used as substrate in a constructed wetland system. Seventeen DWTSs were collected from different areas in the UK to study the combined effect of sludge inherent properties and solution chemistry; and the P equilibrium and kinetic adsorption behaviour using batch experiments. Results revealed that the metal content (Al, Fe, Aloxalate and Feoxalate) and specific surface area components had the most significant explanation for the variance of: (i) P-uptake at different initial P concentrations; (ii) the adsorption maxima; and (iii) the Freundlich constant. Overall, giving the combined effect of intrinsic sludge properties and solution chemistry, dewatered waterworks sludges with high reactive metal content (Al and Fe), Ca and SO42- ions, and total specific surface area, would be the best choice for P retention in practical applications. Phosphorus retention by two Al- and two Fe-DWTS were modelled under various operation conditions of hydraulic retention time and influent P concentration, using a continuous feeding system. Four design equations for P retention were developed and these successfully predicted discrete P retention, maximum P loaded to the sludge, accumulative amount of P retention, and lifespan at the required P saturation degree. The model results revealed that the lifespan of ferric sludge is about four years to reach its saturation point, if the flow rate of 190 (l/capita.d) and inflow P concentration of 5 mg/l are used. IV With regards to coagulant recycling and P recovery using electrodialysis (ED) technology, P saturation degree influenced negatively on Fe and P recovery where their percentages dropped from 70 ± 8%, 49 ± 3% to 17 ± 2, 6 ± 1% when P saturated sludge increase from 0% to 100% respectively. The normalised values of recovered Fe to permeated dissolved organic carbon (DOC) were between 29 and 290. Most of the recovered coagulants were comparable in performance with commercial coagulant in term of DOC removal (42 to 59%), Turbidity, and UV254 absorbance. Overall, the results have shown that DWTS has great potential not only for P removal but also for coagulant and P recovery. However, further research is needed before the developed models can be applied at field scale, and also to enhance the ED recovery for further benefits. | |
| 01/01/2017 00:00:00 | |
| Link to Article | |
| 1.6.3 | Coagulation–flocculation |
| Efficient removal of phosphorus from turbid water using chemical sedimentation by FeCl3 in conjunction with a starch-based flocculant | |
| Abstract Phosphorus removal is an important issue in the field of water and wastewater treatment. In this study, a starch-based flocculant (St-CTA), as an assisting agent, was fed after the application of traditional inorganic precipitant of ferric chloride (FeCl3) to remove inorganic and organic phosphorus from their respective simulated turbid wastewaters. The effects of various influencing factors, including CTA content of St-CTA, dosage, initial pH, initial turbidity, and initial total phosphorus (TP), were investigated systematically. This modified chemical sedimentation process assisted by St-CTA not only showed high efficient in removing TP and turbidity but also evidently reduced the required dosage of FeCl3. This combination exhibited better efficiency in removing organic TP than in removing inorganic TP from water. The synergistic mechanisms of FeCl3 and St-CTA were discussed in detail by combination of apparent removal effects and floc properties. St-CTA exhibits strong charge neutralization and bridging flocculation effects and can thus efficiently aggregate and precipitate various phosphorus and iron complexes previously formed through chemical sedimentation, adsorption, and chelation. Besides, the validation of this combination usage was further confirmed by treating a real wastewater, and half of the required FeCl3 dosage and one third of the total cost were saved after addition of only 0.4 mg/L St-CTA when 90% TP and 95% turbidity were reduced. This study thus provided a novel technique for the diminution of TP and turbidity in turbid wastewater, considerable reduction of FeCl3 dosage and final cost, and lowering of secondary pollution risk. | |
| 03/01/2020 00:00:00 | |
| Link to Article | |
| 1.6.4 | Coagulation–flocculation |
| Recent Advancement of Coagulation–Flocculation and Its Application in Wastewater Treatment | |
| Increasing environmental awareness coupled with more stringent regulation standards has triggered various industries to challenge themselves in seeking appropriate wastewater treatment technologies. Coagulation–flocculation process is regarded as one of the most important and widely used treatment processes of industrial wastewaters due to its simplicity and effectiveness. This paper provides a critical review on recent studies of coagulation–flocculation treatment processes of various industrial wastewaters. The limitations and challenges for the coagulation–flocculation process such as the toxicity and health hazard posed by inorganic coagulants, production of large amount of toxic sludge, ineffectiveness in removing heavy metals and emerging contaminants, increase in effluent color, inefficient pollutant removal using natural coagulants, and complexity of scaling up procedure are presented. In addition, an overview on the influence of process parameters on treatment efficiency is included in this revie... | |
| 04/27/2016 00:00:00 | |
| Link to Article | |
| 1.6.5 | Coagulation–flocculation |
| Recovery of heavy metal ions and recycle of removal agent in the polymer–surfactant aggregate process | |
| Abstract In a previous work, a novel effluent treatment process was developed and applied to remove heavy metal ions from dilute aqueous solutions using polymer–surfactant aggregates (PSAs) (Shen et al., 2015). A subsequent pH adjustment method for the polymer–surfactant aggregate process has been developed to recover the heavy metal ions from the flocculated PSAs into a concentrated solution and to regenerate the PSAs for recycle. The PSA is a colloidal structure that is formed by micelle-like aggregates associating with the oppositely charged polymer chains. The PSA can then bind with heavy metal ions and precipitate out of the solution. In the work presented, the flocs are firstly acidified using a small volume of 0.05 M H 2 SO 4 . The bound metal ion are leached out in 15 min, and pass through a coarse filter to report as a metallic ions solution 20–50 times more concentrated than the original effluent. After the acid leaching, the flocs can be completely dissolved in a small volume of 0.1 M NaOH. This basic polymer and surfactant solution is then reused in the next treatment cycle; meanwhile, the pH of the solution is neutralised by adding H 2 SO 4 . The results show that the removal efficiency of 11.2 ppm Cd(II) solution remains above 97% after 5 cycles without the need for make-up of the removal agent. The recovery efficiencies of Cd(II), Zn(II), and Cr(III) remain above 91%, 86% and 73%, respectively, after 6 cycles. In addition, a MATLAB simulation shows that the accumulations of Na 2 SO 4 are stabilised at 280 ppm after the third cycle. Thus, the pH adjustment method is able to recover and concentrate the metal ions from the flocculated PSAs, and also to regenerate the removal agent such that it can be recycled with little deterioration of removal ability. | |
| 02/01/2016 00:00:00 | |
| Link to Article | |
| 1.6.6 | Coagulation–flocculation |
| Regeneration and reuse of bio-surfactant to produce colloidal gas aphrons for heavy metal ions removal using single and multistage cascade flotation | |
| Abstract Bio-surfactants are commonly used in the treatment of wastewaters due to their favorable characteristics such as biodegradability and low toxicity. In this work, the bio-surfactants are extracted from low cost substrates like Ziziphus spina-christi (ZSC) plant leaves to reduce the cost of production. Thereafter, the bio-surfactant extracts were used for the preparation of colloidal gas aphrons (CGAs) to remove heavy metal ions (Cu 2+ , Pb 2+ ) from aqueous solutions. The molecules extracted from the leaves induced the foaming and detergent properties of the solution. Surface tension and electric conductivity techniques confirmed the formation of critical micelle at 5 wt% surfactant concentration. CGA bubbles were generated using the bio-surfactant extracts and employed in single stage and multistage cascaded flotation units to remove Cu 2+ and Pb 2+ from aqueous solutions. In the single stage flotation, the removal of Pb 2+ and Cu 2+ from the single and equimolar mixed solution were low. However, in the multistage cascade flotation, the removal efficiency of Pb 2+ and Cu 2+ increased significantly to 90.7% and 88.2%, respectively. Interestingly, the collected foamate from the flotation columns was regenerated using calcium alginate adsorbent and reused further to prepare the CGAs. Bio-surfactant solution obtained from the leaves of ZSC proved to be useful in the preparation of CGAs and the treatment of heavy metal containing wastewater. | |
| 04/01/2019 00:00:00 | |
| Link to Article | |
| 1.6.7 | Coagulation–flocculation |
| The role of sulfonated chitosan-based flocculant in the treatment of hematite wastewater containing heavy metals | |
| Abstract Hematite wastewater containing dissolved heavy metals is a potential threat to eco-environment and human health. Flocculation as an efficient and cost effective water treatment technology should be applied in its treatment. A sulfonated chitosan-based flocculant (CS-g-P(AM-AMPS)) was prepared via graft copolymerization. Two synthesis pathways and reaction products with different molecular structure were discovered in processes. CS-g-P(AM-AMPS) possessed the multifarious functional groups that contributed to its excellent performance in hematite wastewater treatment. Bridging, adsorption and entrapment in coagulation-flocculation were enhanced due to CS-g-P(AM-AMPS), and the impressive floc size and high removal efficiency were represented in the treatment as well. Dissolved heavy metals in the wastewater were removed by the chelation of sulfonate group in CS-g-P(AM-AMPS), the adsorption of other functional groups and the co-settlement with flocs. CS-g-P(AM-AMPS) will have the potential application in industrial wastewater treatment for its high flocculation performance, thermal stability and solubility. | |
| 01/01/2020 00:00:00 | |
| Link to Article | |
1.7 biosurfactant
Biosurfactants are amphiphilic molecules which showed application in the food, medical, and cosmetics industries and in bioremediation.
**Highlights:**
* **The MSI 54 lipopeptide biosurfactant was an anionic molecule which showed high affinity toward cationic heavy metals including Pb, Hg, Mn, and Cd.** When MSI 54 lipopeptide biosurfactant was added to heavy metals, this resulted in a white co-precipitate of the metal–biosurfactant complex. The heavy metal remediation efficacy of the biosurfactant at a 2.0 × critical micelle concentration (CMC) showed removal of 75.5% Hg, 97.73% Pb, 89.5% Mn, and 99.93% Cd, respectively, in 1,000 ppm of the respective metal solution. The surface treatment of farm fresh cabbage, carrot, and lettuce with 2.0 × CMC of the lipopeptide showed effective removal of the surface heavy metal contaminants. [\[Paper\]](https://www.frontiersin.org/articles/10.3389/fmicb.2020.00222/full)
* The purpose of this research is to study effectiveness of biosurfactant with concentration=CMC for the removal of heavy metals, lead, zinc and copper in batch washing test under four different biosurfactant production by microbial origin; Pseudomonas putida T1(8), Bacillus subtilis 3K, Acinetobacter sp, and Actinobacillus sp was grown on mineral salt medium that had been already added with 2% concentration of molasses that it is a low cost application. The samples were kept in a shaker 120 rpm at room temperature for 3 days. Biosurfactant has proven its ability as a washing agent in heavy metals removal from sediments, but more research is needed to optimize the process of removal heavy metals.[ \[Art. #ARTNUM\]](#article-96096-2321006402)
* Bio-surfactants are commonly used in the treatment of wastewaters due to their favorable characteristics such as biodegradability and low toxicity. In this work, the bio-surfactants are extracted from low cost substrates like Ziziphus spina-christi (ZSC) plant leaves to reduce the cost of production. Thereafter, **the bio-surfactant extracts were used for the preparation of colloidal gas aphrons (CGAs) to remove heavy metal ions (Cu 2+ , Pb 2+ )** from aqueous solutions. CGA bubbles were generated using the bio-surfactant extracts and employed in single stage and multistage cascaded flotation units to remove Cu 2+ and Pb 2+ from aqueous solutions. In the single stage flotation, the removal of Pb 2+ and Cu 2+ from the single and equimolar mixed solution were low. However, in the multistage cascade flotation, the removal efficiency of Pb 2+ and Cu 2+ increased significantly to 90.7% and 88.2%, respectively. Interestingly, the collected foamate from the flotation columns was regenerated using calcium alginate adsorbent and reused further to prepare the CGAs. Bio-surfactant solution obtained from the leaves of ZSC proved to be useful in the preparation of CGAs and the treatment of heavy metal containing wastewater. [\[Art. #ARTNUM\]](#article-96096-2913233077)
| 1.7.1 | biosurfactant |
|---|---|
| Application of a low-cost biosurfactant in heavy metal remediation processes | |
| The industrial interest in microbial surfactants has intensified in recent years due to the characteristics of these compounds, such as biodegradability, low toxicity, and effectiveness in removing heavy metals and hydrophobic organic compounds from soil and water. This paper describes the production of a biosurfactant by the yeast Candida tropicalis grown in distilled water with 2.5% molasses, 2.5% frying oil and 4% corn steep liquor. The production of the biosurfactant reached 27 g/l in a 50-l bioreactor with a surface tension of 30 mN/m. Surface tension and engine oil emulsification assays demonstrated the stability of biosurfactant under extreme conditions of temperature and pH as well as in the presence of NaCl. Chemical structures of the biosurfactant were identified using GC–MS and NMR. The isolated biosurfactant was characterised as an anionic molecule capable of reducing the surface tension of water from 70 to 30 mN/m at 0.5% of the critical micelle concentration, with no toxic effects on plant seeds or brine shrimp. In tests involving both the crude and isolated biosurfactant for the removal of heavy metals from contaminated sand under dynamic conditions, the removal rates for Zn and Cu ranged from 30 to 80%, while the best removal rate for Pb was 15%. Tests in packed columns also confirmed the ability of biosurfactant to remove Cu and Zn at rates ranging from 45 to 65%. However, lead was not removed under static conditions. The removal kinetics demonstrated that 30 min was sufficient for the removal of metals and a single washing with the biosurfactant achieved greater removal efficiency. The use of the biosurfactant led to a significant reduction in the electrical conductivity of solutions containing heavy metals. The present findings as well as a brief economic analysis suggest the great potential of this agent for industrial remediation processes of soil and water polluted with inorganic contaminants. | |
| 05/04/2018 00:00:00 | |
| Link to Article | |
| 1.7.2 | biosurfactant |
| Recovery of heavy metal ions and recycle of removal agent in the polymer–surfactant aggregate process | |
| Abstract In a previous work, a novel effluent treatment process was developed and applied to remove heavy metal ions from dilute aqueous solutions using polymer–surfactant aggregates (PSAs) (Shen et al., 2015). A subsequent pH adjustment method for the polymer–surfactant aggregate process has been developed to recover the heavy metal ions from the flocculated PSAs into a concentrated solution and to regenerate the PSAs for recycle. The PSA is a colloidal structure that is formed by micelle-like aggregates associating with the oppositely charged polymer chains. The PSA can then bind with heavy metal ions and precipitate out of the solution. In the work presented, the flocs are firstly acidified using a small volume of 0.05 M H 2 SO 4 . The bound metal ion are leached out in 15 min, and pass through a coarse filter to report as a metallic ions solution 20–50 times more concentrated than the original effluent. After the acid leaching, the flocs can be completely dissolved in a small volume of 0.1 M NaOH. This basic polymer and surfactant solution is then reused in the next treatment cycle; meanwhile, the pH of the solution is neutralised by adding H 2 SO 4 . The results show that the removal efficiency of 11.2 ppm Cd(II) solution remains above 97% after 5 cycles without the need for make-up of the removal agent. The recovery efficiencies of Cd(II), Zn(II), and Cr(III) remain above 91%, 86% and 73%, respectively, after 6 cycles. In addition, a MATLAB simulation shows that the accumulations of Na 2 SO 4 are stabilised at 280 ppm after the third cycle. Thus, the pH adjustment method is able to recover and concentrate the metal ions from the flocculated PSAs, and also to regenerate the removal agent such that it can be recycled with little deterioration of removal ability. | |
| 02/01/2016 00:00:00 | |
| Link to Article | |
| 1.7.3 | biosurfactant |
| Regeneration and reuse of bio-surfactant to produce colloidal gas aphrons for heavy metal ions removal using single and multistage cascade flotation | |
| Abstract Bio-surfactants are commonly used in the treatment of wastewaters due to their favorable characteristics such as biodegradability and low toxicity. In this work, the bio-surfactants are extracted from low cost substrates like Ziziphus spina-christi (ZSC) plant leaves to reduce the cost of production. Thereafter, the bio-surfactant extracts were used for the preparation of colloidal gas aphrons (CGAs) to remove heavy metal ions (Cu 2+ , Pb 2+ ) from aqueous solutions. The molecules extracted from the leaves induced the foaming and detergent properties of the solution. Surface tension and electric conductivity techniques confirmed the formation of critical micelle at 5 wt% surfactant concentration. CGA bubbles were generated using the bio-surfactant extracts and employed in single stage and multistage cascaded flotation units to remove Cu 2+ and Pb 2+ from aqueous solutions. In the single stage flotation, the removal of Pb 2+ and Cu 2+ from the single and equimolar mixed solution were low. However, in the multistage cascade flotation, the removal efficiency of Pb 2+ and Cu 2+ increased significantly to 90.7% and 88.2%, respectively. Interestingly, the collected foamate from the flotation columns was regenerated using calcium alginate adsorbent and reused further to prepare the CGAs. Bio-surfactant solution obtained from the leaves of ZSC proved to be useful in the preparation of CGAs and the treatment of heavy metal containing wastewater. | |
| 04/01/2019 00:00:00 | |
| Link to Article | |
| 1.7.4 | biosurfactant |
| Removal of Heavy Metals Pb, Zn and Cu from Sludge Waste of Paper Industries Using Biosurfactant | |
| Increasing public awareness of environmental pollution influences the search and development of technologies that help in cleanup of organic and inorganic contaminants such as metals. Sludge waste of paper industries as toxic and hazardous material from specific source containing Pb, Zn, and Cu metal from waste soluble ink. An alternative and eco-friendly method of remediation technology is the use of biosurfactants and biosurfactant-producing microorganisms. Soil washing is among the methods available to remove heavy metal from sediments. The purpose of this research is to study effectiveness of biosurfactant with concentration=CMC for the removal of heavy metals, lead, zinc and copper in batch washing test under four different biosurfactant production by microbial origin; Pseudomonas putida T1(8), Bacillus subtilis 3K, Acinetobacter sp, and Actinobacillus sp was grown on mineral salt medium that had been already added with 2% concentration of molasses that it is a low cost application. The samples were kept in a shaker 120 rpm at room temperature for 3 days. Supernatants and sediments of sludge were separated by using a centifuge and samples from supernatants were measured by Atomic Absorption Spectrophotometer. The highest removal of Pb was up to 14.04% by Acinetobacter sp. Biosurfactant of Pseudomonas putida T1(8) have the highest removal for Zn and Cu was up to 6.5% and 2.01% respectively. Biosurfactant have a role for removal process of the metals, including wetting, contact of biosurfactant to the surface of the sediments and detachment of the metals from the sediment. Biosurfactant has proven its ability as a washing agent in heavy metals removal from sediments, but more research is needed to optimize the process of removal heavy metals. | |
| 01/01/2014 00:00:00 | |
| Link to Article | |
1.8 Ion exchange
Ion exchange usually describes a processes of purification of aqueous solutions using solid polymeric ion exchange resin. More precisely, the term encompasses a large variety of processes where ions are exchanged between two electrolytes.[\[Wiki\]](https://en.wikipedia.org/wiki/Ion_exchange)
**Highlights:**
* This study aims at using ion-exchange resin to remove heavy metals such as copper, zinc, cadmium, and chromium from sludge generated by a PCB manufacturing plant. The ion-exchange resin plays an important role in the sludge extraction or metal recovery. [\[Art. #ARTNUM\]](#article-96073-2155454150)
* The conventional techniques used for the removal of heavy metals are chemical precipitation, chemical oxidation, coagulation, evaporation, ion exchange, membrane separation, reverse osmosis, electrolytic and adsorption. However, **composite ion exchangers have proven to be versatile and efficient for removing heavy metals from contaminated water.** [\[Art. #ARTNUM\]](#article-96073-2911818693)
* An innovative phosphorus removal filter made of silica granules was designed and evaluated for advanced wastewater treatment. The silica granules from natural mineral stones were formed into a porous body by sintering with addition of glass powder. The phosphorus was removed by the ionic exchange mechanism between OH − in Si(OH) 4 and PO 4 3− in wastewater. The silica filter was very effective in removing phosphorus in wastewater by ion exchange. We found the possibility of a phosphorus removal filter with no sludge production characteristics of flocculation treatment techniques, and it seems to be quite meaningful as a new wastewater treatment. [\[Art. #ARTNUM\]](#article-96073-1970619429)
* Ion exchange is another method used successfully in the industry for the removal of heavy metals from effluent. An ion exchanger is a solid capable of exchanging either cations or anions from the surrounding materials. Commonly used matrices for ion exchange are synthetic organic ion exchange resins. The disadvantage of this method is that it cannot handle concentrated metal solution as the matrix gets easily fouled by organics and other solids in the wastewater. Moreover ion exchange is nonselective and is highly sensitive to the pH of the solution.[\[Paper\]](https://www.sciencedirect.com/science/article/pii/S1878535210001334#:\~:text=2.3.&text=The%20conventional%20processes%20for%20removing,metal%20removal%20from%20inorganic%20effluent.)
| 1.8.1 | Ion exchange |
|---|---|
| Alternative technique for removal of phosphorus in wastewater using chemically surface-modified silica filter | |
| Abstract An innovative phosphorus removal filter made of silica granules was designed and evaluated for advanced wastewater treatment. The silica granules from natural mineral stones were formed into a porous body by sintering with addition of glass powder. The phosphorus was removed by the ionic exchange mechanism between OH − in Si(OH) 4 and PO 4 3− in wastewater. The silica filter was very effective in removing phosphorus in wastewater by ion exchange. We found the possibility of a phosphorus removal filter with no sludge production characteristics of flocculation treatment techniques, and it seems to be quite meaningful as a new wastewater treatment. | |
| 09/01/2012 00:00:00 | |
| Link to Article | |
| 1.8.2 | Ion exchange |
| Biosorption of Heavy Metal by Algae Biomass in Surface Water | |
| Discharging wastewater containing heavy metals of Cu, Pb, Zn and Cd into water bodies can cause toxicity in plants and aquatic animals and some of them will be unable to survive except algae. Wastewater treatment method to remove heavy metal contaminants includes chemical precipitation, ion exchange, membrane, filtration, adsorption using activated carbon. However, these methods are either expensive or have other disadvantages such as high energy consumption and inefficiencies when existing heavy metals are at trace concentration. Biosorption using algae biomass can be an alternative method to eliminate heavy metals. The objective of the project is to investigate the capability of Marine Algae (MA) and Freshwater Algae (FA) bi-omass in adsorbing heavy metals of Cu, Pb, Zn and Cd from water medium using synthetic water and industrial water. MA and FA were obtained from the eastern coast of Pulau Ubin and local fish farm respectively. After being fully washed with deionised water, dried in a furnace for 105°C, they are grinded to pass 1 mm2 of siever. MA and FA were characterised using FTIR to determine their functional groups. An industrial water was collected from industrial discharge from metal fac-tories in northern side of Singapore. Effect of adsorption time, adsorbent concentra-tion, and pH were studied. The result showed that FA and MA had a higher capability in adsorbing a total metal of about 40 ppm level from an industrial water, or 4 times than synthetic water concentration, at the same adsorbent dosage of 50 mg. In con-clusion, the presence of various functional groups, hydroxyl, carboxylic and amine groups, in all MA and FA samples had enabled the algae biomass to adsorb heavy metals of Cu, Pb, Cd and Zn from synthetic and industrial water. Due to their bio-sorptive properties and fast adsorption capability, algae could be a potential method for cleaning up surface water or post-treatment of wastewater and minimise the cost of eutrophication. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 1.8.3 | Ion exchange |
| Factorial experimental design for recovering heavy metals from sludge with ion-exchange resin | |
| Wastewaters containing heavy metals are usually treated by chemical precipitation method in Taiwan. This method can remove heavy metals form wastewaters efficiently, but the resultant heavy metal sludge is classified as hazardous solid waste and becomes another environmental problem. If we can remove heavy metals from sludge, it becomes non-hazardous waste and the treatment cost can be greatly reduced. This study aims at using ion-exchange resin to remove heavy metals such as copper, zinc, cadmium, and chromium from sludge generated by a PCB manufacturing plant. Factorial experimental design methodology was used to study the heavy metal removal efficiency. The total metal concentrations in the sludge, resin, and solution phases were measured respectively after 30 min reaction with varying leaching agents (citric acid and nitric acid); ion-exchange resins (Amberlite IRC-718 and IR-120), and temperatures (50 and 70 °C). The experimental results and statistical analysis show that a stronger leaching acid and a higher temperature both favor lower heavy metal residues in the sludge. Two-factors and even three-factor interaction effects on the heavy metal sorption in the resin phase are not negligible. The ion-exchange resin plays an important role in the sludge extraction or metal recovery. Empirical regression models were also obtained and used to predict the heavy metal profiles with satisfactory results. | |
| 12/01/2006 00:00:00 | |
| Link to Article | |
| 1.8.4 | Ion exchange |
| Sequestration of Heavy Metals from Industrial Wastewater Using Composite Ion Exchangers | |
| The transition from agrarian to an industrial society has witnessed several environmental concerns globally. In recent years, contamination of water bodies with refractory contaminants discharged from industrial wastewater significantly interrupted the ecosystems. The most important pollutants in surface and groundwater are arsenic, cadmium, chromium, copper, lead, mercury, nickel and zinc; the recalcitrant pollutant and bioaccumulate in the ecosystems as metal–organic complexes. The conventional techniques used for the removal of heavy metals are chemical precipitation, chemical oxidation, coagulation, evaporation, ion exchange, membrane separation, reverse osmosis, electrolytic and adsorption. However, composite ion exchangers have proven to be versatile and efficient for removing heavy metals from contaminated water. This chapter focuses on various materials (inorganic to nanocomposite) recently developed for the removal of heavy metals from wastewater, mechanisms and treatment performance. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
1.9 Ion flotation
Ion flotation is a separation technology for recovering and removing metal ions from dilute aqueous solutions. In this process, an ionic collector is utilized to transport non-surface active colligend ions of the opposite charge from a bulk solution to the solution–vapor interface.[\[Paper\]](https://www.sciencedirect.com/science/article/pii/S0301751603001133#:\~:text=Ion%20flotation%20is%20a%20separation,to%20the%20solution%E2%80%93vapor%20interface.)
**Highlights:**
* Ion flotation is a promising process for the separation of toxic metals from industrial wastewater. It is a separation and elimination process for the treatment of surface-inactive ions from the aqueous media by the addition of a surfactant which has an opposite charge to the removal metal ion. When the surfactants are added into the industrial effluent, the metal ion is transferring into the hydrophobic phase. These metal ions in the hydrophobic phase react with air bubbles to form flocks and elimination of flocks takes place respectively. Ion flotation technique was employed for the remediation of toxic heavy metal ions from an aqueous solution which has little concentration. [\[Paper\]](https://www.researchgate.net/publication/331952883_Remediation_of_Nickel_ion_from_wastewater_by_applying_various_techniques_a_review)
* The objective of the present work is to extend the application of adsorbing colloid flotation techniques to remove mixtures of metal ions. The systems studied are: 1) Co(II) and Cr(VI); 2) Co(II), Ni(II), and Cr(VI); 3) Cr(VI), Cu(II), and Zn(II); 4) Cr(VI), Cu(II), Zn(II), and Ni(II); 5) Cd(II), Pd(II), and Cu(II). Ferric hydroxide and aluminum hydroxide were used as the coprecipitant, and sodium lauryl sulfate was used as the collector and frother. The ionic strength of the solution was adjusted with NaNO3 or Na2SO4. It was found that all the heavy metals can be removed effectively by a single step foam flotation treatment. [\[Art. #ARTNUM\]](#article-96231-2028743979)
| 1.9.1 | Ion flotation |
|---|---|
| Simutaneous Removal of Heavy Metal Ions from Wastewater by Foam Separation Techniques | |
| Abstract The objective of the present work is to extend the application of adsorbing colloid flotation techniques to remove mixtures of metal ions. The systems studied are: 1) Co(II) and Cr(VI); 2) Co(II), Ni(II), and Cr(VI); 3) Cr(VI), Cu(II), and Zn(II); 4) Cr(VI), Cu(II), Zn(II), and Ni(II); 5) Cd(II), Pd(II), and Cu(II). Ferric hydroxide and aluminum hydroxide were used as the coprecipitant, and sodium lauryl sulfate was used as the collector and frother. The ionic strength of the solution was adjusted with NaNO3 or Na2SO4. It was found that all the heavy metals can be removed effectively by a single step foam flotation treatment. | |
| 04/01/1988 00:00:00 | |
| Link to Article | |
1.10 (Advanced) Oxidation processes
Advanced oxidation processes (AOPs), in a broad sense, are a set of chemical treatment procedures designed to remove organic (and sometimes inorganic) materials in water and wastewater by oxidation through reactions with hydroxyl radicals (·OH). In real-world applications of wastewater treatment, however, this term usually refers more specifically to a subset of such chemical processes that employ ozone (O3), hydrogen peroxide (H2O2) and/or UV light.[\[Wiki\]](https://en.wikipedia.org/wiki/Advanced_oxidation_process)
To remove various toxic and hazardous chemicals especially endocrine-disrupting chemicals from wastewater, chemical oxidation techniques are preferred, and it is a promising technology for the treatment of wastewaters containing pharmaceuticals products. Organic compounds that are oxidized by oxidation of readily degradable species such as alcohols and carboxylic acids are the main components of this process. Ozone, hydrogen peroxide, and Fenton’s reagent are commonly used as chemical oxidation reagent.[\[Paper\]](https://www.intechopen.com/online-first/heavy-metal-removal-techniques-using-response-surface-methodology-water-wastewater-treatment)
* When Ca(ClO)₂ and CaO₂ were applied, an increase of the supernatant conductivity was achieved. COD removal ≥71% and turbidity elimination in the range of 85–100% were achieved by using oxidation processes. CaO₂ was very effective to remove total phosphorus (81–96%). The increase of the oxidant concentration in H2O2 and Ca(ClO)₂ oxidation processes led to a decrease in the removal of total phenols and bicarbonates species. Optical density of the microorganism cultures was efficiently eliminated (up to 100%) by oxidation processes. [\[Art. #ARTNUM\]](#article-96289-2974412099)
* Therefore, the aim of this study is to remove heavy lead metal from aqueous solution by Fenton method. This study is an experimental study. The samples are synthesized in a collection of laboratories at the Faculty of Health, and the pH parameters, contact time and lead elimination rate and the optimal Fenton ratio are investigated. Results are analyzed using SPSS software and Charts are plotted by excel. The results showed that the best pH for removal of lead 5 and its best concentration is 30 mg/ L, and the optimal Fenton ratio is 1 to 5, as well as the best contact time for removal of lead from aqueous media for 10 minutes. The present study showed that the pH factor, contact time, Fenton concentration and lead in all four were effective in removing lead from aquatic solution.[\[Paper\]](http://www.journalcsij.com/index.php/CSIJ/article/view/30111)
* Phosphoric acid of 8% concentration with hydrogen peroxide showed good removal rates of heavy metals comparable to those by 1 N hydrochloric acid. Copper is easily removed from the sludge in the presence of hydrogen peroxide. From the results of the investigation of the solubilities of several copper compounds into phosphoric acid with or without hydrogen peroxide, the copper in the sludge does not exist as copper sulfides, but it seems to exist as copper thiolates containing Cu(I) in biopolymers. In this process, the phosphoric acid used for the removal of heavy metals is almost entirely recovered and is reused. Sewage sludge with low content of heavy metals can be recycled as a useful resource.[\[Paper\]](https://www.researchgate.net/publication/231292183_Principle_and_Process_of_Heavy_Metal_Removal_from_Sewage_Sludge)
| 1.10.1 | (Advanced) Oxidation processes |
|---|---|
| Treatment of slaughterhouse wastewater by acid precipitation (H2SO4, HCl and HNO3) and oxidation (Ca(ClO)₂, H2O2 and CaO₂) | |
| Abstract The treatment of slaughterhouse wastewater was investigated by both acid precipitations and by oxidation processes. Precipitation tests were developed using three acids (H2SO4, HCl and HNO3) at different operating pH (1–6). A decrease of the precipitation pH led to an increase of the conductivity values of the supernatant. Precipitation processes allowed the removal of chemical oxygen demand (COD) (41–97%), turbidity (56–99%) and total phosphorus (27–56%). Total phenols were removed (15–96%) from pH ≥ 2, depending on the precipitation process. Generally, precipitation processes decreased the hydroxide and bicarbonates species. Additionally, three different oxidation processes were tested at different concentrations (1–15 g L−1): Ca(ClO)₂, H2O2 and CaO₂. When Ca(ClO)₂ and CaO₂ were applied, an increase of the supernatant conductivity was achieved. COD removal ≥71% and turbidity elimination in the range of 85–100% were achieved by using oxidation processes. CaO₂ was very effective to remove total phosphorus (81–96%). The increase of the oxidant concentration in H2O2 and Ca(ClO)₂ oxidation processes led to a decrease in the removal of total phenols and bicarbonates species. Optical density of the microorganism cultures was efficiently eliminated (up to 100%) by oxidation processes. In addition, acid precipitation and oxidation allowed to remove total solids (TS), total volatile solids (TVS), total suspended solids (TSS), ammonia nitrogen, nitrates and biochemical oxygen demand (BOD5). Acid precipitation and oxidation produced sludge rich in organic matter and nutrients (Ca, Mg, P, Cl, Na and K). Despite the high removal efficiencies, a post-treatment following the precipitation and oxidation processes can be required. | |
| 11/01/2019 00:00:00 | |
| Link to Article | |
2. Sorption materials
BackMaterials that ab/adsorb contaminants physically or chemically.
2.1 Activated carbon
Activated carbon, also called activated charcoal, is a form of carbon processed to have small, low-volume pores that increase the surface area available for adsorption or chemical reactions.[\[Wiki\]](https://en.wikipedia.org/wiki/Activated_carbon#:\~:text=Activated%20carbon%2C%20also%20called%20activated,is%20sometimes%20substituted%20with%20active.)
Activated carbons have been used in many adsorption processes, among which nutrient removal and heavy metal removal.
**Highlights:**
* The effect of temperature and contact time on the removal of these heavy metals using the activated carbon produced was investigated. The activated carbon showed a significant ability in removing heavy metals; Cadmium, Copper, Nickel, and Lead from the wastewater. [\[Paper\]](https://link.springer.com/article/10.1007/s13201-016-0460-x#:\~:text=The%20effect%20of%20temperature%20and,and%20Lead%20from%20the%20wastewater.)
* Batch experiments were conducted to test the ability of activated carbon for the removal of lead, cadmium, nickel, chromium and zinc from water. Nickel showed the highest removal percentages by activated carbon at all concentrations and the removal percentages decreased as the concentration of heavy metal increased. [\[Paper\]](https://www.sciencedirect.com/science/article/pii/S1876610214007504)
* Nutrients (P, N) in stormwater runoff are a major cause of eutrophication and algal blooms. **A promising solution to this problem is to amend the rain garden growing medium (RGGM) with sewage sludge-based activated carbon (SBAC).** To optimize the SBAC production process, different metals, pyrolysis conditions (temperature, heating time, carrier gas), and post-treatments were explored. When pyrolyzed at 400 °C for two hours, Zn-activated SBAC removed up to 41% of PO4-P (initial concentration of 1 mg/L) and 72% of NO3-N (initial concentration of 2 mg/L), at a dose of 1 g sorbent/L of nutrient-spiked distilled water. When the same dosage was applied to stormwater leachate made from RGGM and spiked with nutrients, the removal efficiencies were reduced to 20% for PO4-P and 38% for NO3-N. [\[Paper\]](https://www.sciencedirect.com/science/article/pii/S0301479718308521)
| 2.1.1 | Activated carbon |
|---|---|
| Biosorption of Heavy Metal by Algae Biomass in Surface Water | |
| Discharging wastewater containing heavy metals of Cu, Pb, Zn and Cd into water bodies can cause toxicity in plants and aquatic animals and some of them will be unable to survive except algae. Wastewater treatment method to remove heavy metal contaminants includes chemical precipitation, ion exchange, membrane, filtration, adsorption using activated carbon. However, these methods are either expensive or have other disadvantages such as high energy consumption and inefficiencies when existing heavy metals are at trace concentration. Biosorption using algae biomass can be an alternative method to eliminate heavy metals. The objective of the project is to investigate the capability of Marine Algae (MA) and Freshwater Algae (FA) bi-omass in adsorbing heavy metals of Cu, Pb, Zn and Cd from water medium using synthetic water and industrial water. MA and FA were obtained from the eastern coast of Pulau Ubin and local fish farm respectively. After being fully washed with deionised water, dried in a furnace for 105°C, they are grinded to pass 1 mm2 of siever. MA and FA were characterised using FTIR to determine their functional groups. An industrial water was collected from industrial discharge from metal fac-tories in northern side of Singapore. Effect of adsorption time, adsorbent concentra-tion, and pH were studied. The result showed that FA and MA had a higher capability in adsorbing a total metal of about 40 ppm level from an industrial water, or 4 times than synthetic water concentration, at the same adsorbent dosage of 50 mg. In con-clusion, the presence of various functional groups, hydroxyl, carboxylic and amine groups, in all MA and FA samples had enabled the algae biomass to adsorb heavy metals of Cu, Pb, Cd and Zn from synthetic and industrial water. Due to their bio-sorptive properties and fast adsorption capability, algae could be a potential method for cleaning up surface water or post-treatment of wastewater and minimise the cost of eutrophication. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 2.1.2 | Activated carbon |
| Selective removal of heavy metals from landfill leachate by reactive granular filters | |
| Abstract The pre-treatment of landfill leachate prior to its co-treatment in the municipal plants of waste water processing could represent an appropriate and cost-effective solution for its management. Pre-treatment is necessary especially to remove heavy metals, which may be transferred to the excess sludge preventing its valorisation. In the present paper, we propose a chemical-physical pre-treatment of leachate using four different granular reactive media able to selectively remove the contaminants present in the leachate. The efficiency of these materials was investigated using synthetic leachate through batch tests and a column test. In the latter case the four materials were placed in two columns connected in series and fed an under constant upward flow (0.5 mL/min). The first column was filled half (50 cm) with a granular mixture of zero valent iron (ZVI) and pumice and half (50 cm) with a granular mixture of ZVI and granular activated carbon (GAC). The second column, which was fed with the effluent of the first column, was filled half with zeolite (chabazite) and half with GAC. Heavy metals were mainly removed by the ZVI/pumice and ZVI/GAC steps with a removal efficiency that was higher than 98, 94 and 90% for copper, nickel and zinc, respectively, after 70 days of operation. Ammonium was removed by zeolite with a removal efficiency of 99% up to 23 days. The average reduction of the chemical oxygen demand (COD) was of 40% for 85 days, whereas chloride and sulphate removal was negligible. | |
| 12/01/2018 00:00:00 | |
| Link to Article | |
2.2 Ashes
Ashes (such as fly ash or biomass ash), are a common byproduct of thermochemical processes.
**Highlights:**
* Fly ash had been widely used in the process of sewage treatment due to its wide source,high porosity structure,large surface area and so on. It has been cleared about the application value of fly ash in removing heavy metals,which lay the foundation for the comprehensive investigation of fly ash on heavy metals treatment in the future.[ \[Art. #ARTNUM\]](#article-96094-2376033866)
* **Adsorption of Chromium and lead ions onto sewage sludge ash from aqueous solutions** was studied to enable comparison with alternative commonly available absorbents. Highest metal uptake of 45 and 62 mg/g were observed for Cr and Pb, respectively. Pb showed higher affinity and adsorption rate compared to Cr under all the experimental conditions. Kinetic studies revealed that Pb and Cr uptake was up with 90% or more of the adsorption occurring at 60 min of contact time. [\[Paper\]](https://papers.ssrn.com/sol3/papers.cfm?abstract_id=3164094)
* This work studied the effectiveness of fly ash in removing phosphate from aqueous solution and its related removal mechanism. **The adsorption and precipitation of phosphate by fly ash** were investigated separately in order to evaluate their role in the removal of phosphate. Results showed that the removal of phosphate by fly ash was rapid. The removal percentage of phosphate in the first 5min reached 68-96% of the maximum removal of phosphate by fly ash. The removal processes of phosphate by fly ash included a fast and large removal representing precipitation, then a slower and longer removal due to adsorption. [\[Paper\]](https://pubmed.ncbi.nlm.nih.gov/18434007/#:\~:text=Therefore%2C%20the%20removal%20of%20phosphate,wastewater%20treatment%20and%20pollution%20control.)
| 2.2.1 | Ashes |
|---|---|
| Characteristics of Fly Ash and Its Study Progress in Removing Heavy Metals in Wastewater | |
| Fly ash had been widely used in the process of sewage treatment due to its wide source,high porosity structure,large surface area and so on. The characteristics and mineral composition of fly ash were analyzed in this paper. The adsorption mechanism of fly ash was discussed. The current situations of fly ash in removing heavy metals in wastewater was elaborated. The performance of different methods of modified fly ash adsorb heavy metals was announced. It has been cleared about the application value of fly ash in removing heavy metals,which lay the foundation for the comprehensive investigation of fly ash on heavy metals treatment in the future. | |
| 01/01/2015 00:00:00 | |
| Link to Article | |
| 2.2.2 | Ashes |
| Porous fly ash-based geopolymer composite fiber as an adsorbent for removal of heavy metal ions from wastewater | |
| Abstract This paper describes a simple and effective process for fabricating geopolymer-polymer composite fiber. The fiber is synthesized by mixing geopolymer powder with Polyethersulfone (PES) – N -Methyl-2 pyrrolidone (NMP) solution and the slurry was extruded then transformed into a fiber by phase inversion method. The fiber is constructed of PES and fly ash-based geopolymer (FAG) particles with porous structure. Analysis of the pore structure of fiber revealed that BET surface area is 168.30 m 2 /g. In addition, the adsorption capacity of heavy metal ions on geopolymer composite fiber follows the order of Pb 2+ > Cu 2+ > Cd 2+ > Ni 2+ . This work provides a convenient, low-cost and environmental friendly adsorbent for removing heavy metal ions from waste water. | |
| 02/01/2019 00:00:00 | |
| Link to Article | |
| 2.2.3 | Ashes |
| Study of a Chilean petroleum coke fluidized bed combustion fly ash and its potential application in copper, lead and hexavalent chromium removal | |
| Abstract This work deals with the characterization of a circulated fluidized bed combustion (CFCB) Chilean petroleum coke fly ash (FA) from a petroleum coke power plant, and its potential use in neutralization and heavy metals removal from acid wastewaters. FA presents a high Ca and SO 4 2 - content, being anhydrite the major crystalline mineral phase, with minor proportions of calcite, portlandite and lime. Regarding to environmental characterization of this fly ash, leaching tests allowed concluding that FA is a non-hazardous residue. Heavy metals removal tests indicate that FA is able to remove Cu 2+ and Pb 2+ mainly due to a precipitation process, while Cr(VI) is being removed probably due to a reduction process to Cr(III), at high liquid to solid ratios. Cu 2+ , Pb 2+ and Cr(VI) kinetic experimental data present acceptable fit to a pseudo-second order kinetic model. According to these results, FA may be used to remove heavy metals and neutralize acid wastewaters, suggesting a possible replacement of pure and costly alkaline materials. | |
| 10/01/2010 00:00:00 | |
| Link to Article | |
2.3 Clays and minerals
Clays and different types of minerals have been used as sorbent and ion exchangers. Other types of mineral compounds are zeolites, brick materials, and concrete-like materials.
**Highlights:**
* **Vermiculite is a kind of clay mineral which has big specific surface area and strong cation exchange capacity and can effectively remove heavy metal ions from wastewater.** It was pointed out that, it should deepen the study of the vermiculite adsorption mechanism and the disposal technology after the adsorption, and promote the application of vermiculite in actual projects. [\[Art. #ARTNUM\]](#article-96084-2391872728)
* The highest adsorption capacity (q = 4.92 mg/g) of ammonium ions with the maximum removal efficiency (52.3%) was obtained for bentonite, with a 0–0.05 mm particle size. After pretreatment with a 1 mol/L NaCl solution, maximum efficiency increments were observed (55.7%). **Based on these results it was concluded that natural sorbents may be effectively applied in wastewater treatment.** [\[Art. #ARTNUM\]](#article-96084-2979571471)
* In this study, **zeolite adsorption** and anaerobic digestion (AD) were integrated to improve the methane production and energy recovery of PHWW from Chlorella 1067. A statistical design for maximum toxicants removal by zeolite was applied before AD process. Zeolite could mitigate the inhibition associated to compounds such as ammonia, N-heterocyclic compounds, etc. in PHWW and thereby shortening the lag phase and increasing methane production by 32–117% compared with that without zeolite adsorption. Zeolite adsorption also increased energy recovery efficiency (up to 70.5%) for this integrated system. Integration of HTL and AD brought higher energetic return from feedstock via oil and biomethane production, which may offer insight into industrial application of microalgae biomass in the circular economy. In addition, carbon and nitrogen flow for the integrated process was determined. [\[Paper\]](https://www.sciencedirect.com/science/article/pii/S0048969718336192?via%3Dihub)
* In this paper, a batch experiment was conducted to evaluate the water quality obtained from **using pervious concrete (PERVC) technology to treat acid mine drainage (AMD).** [\[Art. #ARTNUM\]](#article-96084-2982363937)
| 2.3.1 | Clays and minerals |
|---|---|
| A critical review of clay-based composites with enhanced adsorption performance for metal and organic pollutants | |
| Abstract Adsorption techniques offer unique advantages owing to the use of synthetic (e.g., nanosized metal oxides and polymer-functionalized nanocomposites) and natural (e.g., clay and biochar) materials for pollutant removal. Although the most widely used adsorbent is activated carbon, extensive studies have highlighted the promising potential of modified clay minerals and biochar for removing heavy metal and organic pollutants from industrial, drinking, and eutrophic wastewater, due to their low cost and easy accessibility. However, clay modification using acids, calcination, polymers, or surfactants exhibits relatively low absorption/regeneration ability towards antibiotics, aromatics, and various dyes. The coexistence of numerous contaminants in industrial wastewater inhibited the performance of adsorbents, which accelerated the development of novel modified clay composites such as clay-biochar, organo-bentonite/sodium alginate beads, and enhanced biochar. This review summarizes recent studies and absorption mechanisms concerning clay composites based on various modification methods and component materials. The comparison of clay composites used for the removal of organic and inorganic contaminants provides valuable insight into real wastewater treatment. Knowledge gaps, uncertainties, and future challenges involved in the fabrication and regeneration of modified clay composites are also identified. | |
| 02/01/2019 00:00:00 | |
| Link to Article | |
| 2.3.2 | Clays and minerals |
| Alginate clay hybrid composite adsorbents for the reclamation of industrial lean methyldiethanolamine solutions | |
| Abstract Alginate based clay hybrid composites were used as adsorbents for the removal of total organic acid anions (TOA) as heat stable salt (HSS) and heavy metal ions (chromium and iron) from industrial lean methyldiethanolamine (MDEA, 50 wt%) solvents. Spherical calcium alginate based hybrid (CAH) composites were prepared using three different filler clays such as sepiolite, montmorillonite and bentonite. To overcome the inherent iron leaching problem associated with clay minerals, an appropriate clay treatment method was utilized before preparing the hydrogel composite. The structure of the clay (before and after modification) and composites was characterized by XRD, whereas the sorption mechanism of the CAH hydrogel composites was conferred in combination with the results obtained from SEM, EDX and FTIR analyses. The effect of quantitative contributions of polymer, bead size, agitation speed, cross linker concentration, reaction time and filler weight% were studied using batch adsorption. The initial experiments confirmed that all the hybrid composites could superiorly separate HSS and heavy metal ions from lean MDEA solvents. 2.0 wt% clay containing composite hydrogels prepared by using 1 mm dropper in a CaCl 2 solution of 1.5 M was found to have highest adsorption capacity. Thus, calcium alginate hybrid (CAH) composites showed efficient adsorption capacity for removing all the contaminants present in lean MDEA. | |
| 02/01/2018 00:00:00 | |
| Link to Article | |
| 2.3.3 | Clays and minerals |
| Amorphous Phosphated Titanium Oxide with Amino and Hydroxyl Bifunctional Groups for Highly Efficient Heavy Metals Removal | |
| Heavy metals pollution in water has become one of the main environmental problems in today's society. Currently, the traditional adsorbents can hardly adsorb heavy metals in wastewater to trace levels meeting the standards of drinking water. It is an urgent task to design and construct new adsorption materials for effectively removing heavy metals from sewage to reach trace levels. Herein, a new adsorbent of functional amorphous phosphated titanium oxide (FAPTO) anchoring organic (-NH2/-NH-) and inorganic (-OH) bifunctional groups on the surface has been synthesized via a simple one-pot solvothermal approach. The amino as well as hydroxyl groups within the matrix can offer sorption positions for powerful heavy metals capture. The obtained FAPTO can effectively adsorb the heavy metals with the uptake efficiency up to 99.0 %, and remarkably reduce Pb2+, Cd2+, Cr3+ and Fe3+ concentration from ppm levels (~5 mg/L) to ppb levels (0.001-0.04 mg/L) reaching the drinking water standard enacted by World Health Organization. Moreover, the Langmuir equilibrium isotherm indicates that the maximum sorption capacities of FAPTO for Pb2+, Cd2+, Cr3+, and Fe3+ are 761.3, 193.3, 255.2, and 166.1 mg/g, respectively. Importantly, the superior adsorbent of FAPTO possesses the excellent reusability with negligible degradation after multiple reuse. The as-prepared FAPTO could be a promising absorbent for heavy metals removal by virtue of outstanding adsorption performance and eco-friendly fabrication process. | |
| 03/06/2020 00:00:00 | |
| Link to Article | |
| 2.3.4 | Clays and minerals |
| Application of vermiculite in treatment of heavy metal ion-containing wastewater | |
| Vermiculite is a kind of clay mineral which has big specific surface area and strong cation exchange capacity and can effectively remove heavy metal ions from wastewater.The research status on vermiculite adsorbing heavy metal ions such as Cu2+, Cd2+, Ni2+, Pb2+ and so on were summarized, it was found that, the main mechanism of vermiculite removing heavy metal ions were ion exchange and surface complexation.The influences of solution pH value, adsorption time, granular diameter and dosage of vermiculite, solution concentration on the adsorption effect were analyzed.It was pointed out that, it should deepen the study of the vermiculite adsorption mechanism and the disposal technology after the adsorption, and promote the application of vermiculite in actual projects. | |
| 01/01/2009 00:00:00 | |
| Link to Article | |
| 2.3.5 | Clays and minerals |
| Quality of water recovered by treating acid mine drainage using pervious concrete adsorbent | |
| In this paper, a batch experiment was conducted to evaluate the water quality obtained from using pervious concrete (PERVC) technology to treat acid mine drainage (AMD). The study proposes an innovative application of PERVC as a permeable reactive barrier liner in evaporation ponds. The effectiveness of PERVC adsorbent in removing heavy metals was compared with that of zero-valent iron (ZVI) of particle size 1.0 to 1.8 mm. The AMD used in the study was obtained from abandoned gold and coal mines. PERVC mixtures consisted of granite aggregate and ordinary Portland cement CEM I 52.5R (CEM I) or CEM I containing Class F 30% fly ash (30%FA) as a cement replacement material. ZVI was prepared from a mixture of silica sand and iron grit of specific sizes. PERVC and ZVI media were used to conduct batch reactor tests with AMD, for a period of 43 days at a ratio of 1 L of reactive material to 3 L of AMD. The quality of treated AMD was compared against effluent discharge standards. The contaminants Al, Fe and Zn were effectively removed by both PERVC and ZVI. Also, both adsorbents reduced Ni, Co and Cu to levels below those measured in raw AMD. However, PERVC was more effective in removing Mn and Mg while ZVI was ineffective. Although PERVC removed more heavy metals and with greater efficiency than ZVI, the PERVC-treated water showed high pH levels and exhibited elevated Cr6+ concentrations, owing to leaching from the cement and fly ash materials used in PERVC mixtures. | |
| 10/29/2019 00:00:00 | |
| Link to Article | |
| 2.3.6 | Clays and minerals |
| Removal of Ammonia from the Municipal Waste Treatment Effluents using Natural Minerals | |
| Due to various ecological problems, it is required to remove the ammonia nitrogen from wastewater. Industrial wastewater that was not subjected to any purification was used in this study, while most processes described in the literature were carried out using synthetically prepared solutions. The study investigated the removal of ammonium ions using ion exchange on various commercial minerals, in 3 h long batch ion-exchange experiments. Furthermore, research on the sodium chloride activation of the selected mineral was conducted. The screening of the mineral with the highest removal potential was conducted taking into account the adsorption capacity (q) and maximal removal efficiency (E), based on the NH4+ ions changes determined using the selective electrode and spectrophotometric cuvette tests. The highest adsorption capacity (q = 4.92 mg/g) of ammonium ions with the maximum removal efficiency (52.3%) was obtained for bentonite, with a 0–0.05 mm particle size. After pretreatment with a 1 mol/L NaCl solution, maximum efficiency increments were observed (55.7%). The Langmuir adsorption isotherm corresponds well with the equilibrium adsorption data (R2 from 0.97 to 0.98), while the Freundlich model was found to be mismatched (R2 = 0.77). Based on these results it was concluded that natural sorbents may be effectively applied in wastewater treatment. It can be observed that as the size of sorbent particles gets lower, the adsorption capacity, as well as the removal efficiency, gets higher. The bentonite pretreatment with the NaCl solution did not result in the expected efficiency improvement. The 2 mol/L solution affected about 3.5% of the removal efficiency yield. | |
| 10/09/2019 00:00:00 | |
| Link to Article | |
| 2.3.7 | Clays and minerals |
| Removal of Heavy Metals from Industrial Wastewater Through Minerals | |
| Heavy metals are toxic to the health and environment and causes harmful consequences to human beings. It is essential to take effective measures to remove metals from contaminated water. In this research, naturally available brick materials with different compositions collected from Kandy (type A), Gampaha (type B), and Embilipitiya (type C) areas were used to remove Cu, Cr and Pb ions. These brick materials are cost effective and are a readily available alternative to conventional heavy metal removal. The characterization of brick material is performed using X-Ray Fluorescence (XRF) and Nitrogen Adsorption – Desorption analyser. Calculated surface area and total pore volume and pore width of type A, B, and C are lie respectively, in the range of 128–154 m2/g, 0.24–0.45 cm3/g, and 5.6–16.7 nm. The main objective of this research is to investigate how the characteristics of adsorbents influences the adsorption process and to identify the best model to describe the kinetic and equilibrium adsorption to purify metal contaminated water. Results indicate that Pseudo – first – order kinetics model properly described the adsorption of Cu2+ to the brick type C, which has maximum adsorption capacity of 497 mg g−1. The adsorption process of Pb2+ to the brick type A and Cu2+ and Pb2+ to brick type B and C were well-fitted with Pseudo – second – order kinetics model. In equilibrium studies, the Langmuir isotherm showed a better fitness in adsorption of Cu2+ into brick type A and C, Pb2+ into brick type B, whereas the Freundlich isotherm well represented the adsorption characteristics of Cu2+ into brick type A, Pb2+ into brick type B and Cr6+ into all brick types. The comparison of results indicated that the use of brick types A, B, C can be used as a potential nan sorbent to remove heavy metals from industrial waste water. | |
| 12/13/2018 00:00:00 | |
| Link to Article | |
| 2.3.8 | Clays and minerals |
| Selective removal of heavy metals from landfill leachate by reactive granular filters | |
| Abstract The pre-treatment of landfill leachate prior to its co-treatment in the municipal plants of waste water processing could represent an appropriate and cost-effective solution for its management. Pre-treatment is necessary especially to remove heavy metals, which may be transferred to the excess sludge preventing its valorisation. In the present paper, we propose a chemical-physical pre-treatment of leachate using four different granular reactive media able to selectively remove the contaminants present in the leachate. The efficiency of these materials was investigated using synthetic leachate through batch tests and a column test. In the latter case the four materials were placed in two columns connected in series and fed an under constant upward flow (0.5 mL/min). The first column was filled half (50 cm) with a granular mixture of zero valent iron (ZVI) and pumice and half (50 cm) with a granular mixture of ZVI and granular activated carbon (GAC). The second column, which was fed with the effluent of the first column, was filled half with zeolite (chabazite) and half with GAC. Heavy metals were mainly removed by the ZVI/pumice and ZVI/GAC steps with a removal efficiency that was higher than 98, 94 and 90% for copper, nickel and zinc, respectively, after 70 days of operation. Ammonium was removed by zeolite with a removal efficiency of 99% up to 23 days. The average reduction of the chemical oxygen demand (COD) was of 40% for 85 days, whereas chloride and sulphate removal was negligible. | |
| 12/01/2018 00:00:00 | |
| Link to Article | |
2.4 Hydrotalcite
**Hydrotalcite** is a Layered Double Hydroxide whose name is derived from its resemblance with talc and its high water content. Layered double hydroxides (LDH) comprise an unusual class of layered materials with positively charged hydroxide layers and charge balancing, mobile anions located in the interlayer region.[\[Source\]](https://www.kisuma.com/materials/hydrotalcite#:\~:text=Hydrotalcite%20is%20a%20Layered%20Double,located%20in%20the%20interlayer%20region.)
**Highlights:**
* Hydrotalcite materials are generally utilized for anionic pollutants due to its interlayered anion exchange ability. Their potentiality for cationic contaminants is rarely explored. In this study, **disulfide (S2-) intercalated LDH material demonstrated capability to remove both heavy metal cations and oxyanions simultaneously from water.** The S2- intercalation of LDH significantly improved its adsorption capability towards both heavy metal cations (Co2+ and Ni2+) and oxyanion (CrO4 2-). This work provided a highly practical adsorption technology based on the S2- modification hydrotalcite material for the purification of heavy metal ions contaminated wastewater.[ \[Art. #ARTNUM\]](#article-96083-2971605206)
* Hydrotalcites are minerals, sometimes found in stomach antacids, which are able to absorb a variety of contaminants including arsenic, cadmium, and iron. We found that hydrotalcites could be formed by adjusting the concentrations of common wastewater contaminants, aluminium and magnesium, to an ideal ratio, and increasing the pH.[\[Virtual curtain\]](https://www.csiro.au/en/Research/MRF/Areas/Community-and-environment/Minesite-environmental-management/Virtual-curtain)
* A ZnO-ZnAl hydrotalcite (ZZA) was prepared by a new centrifugal method \[...\]. The adsorption by ZZA of phosphate in a simulated wastewater was studied in detail. [\[Paper\]](https://www.tandfonline.com/doi/abs/10.1080/03067319.2019.1622696?journalCode=geac20)
* Hydrotalcites (HT*x*) of different Mg/Al ratio (*x* was Mg/Al ratio; 2, 3, 4) were synthesized by co-precipitation method. Calcined hydrotalcites (CHT*x*) at 500 °C have been shown to recover their original layered structure by **adsorbing nitrate or nitrite from aqueous solution.** [\[Paper\]](https://www.sciencedirect.com/science/article/abs/pii/S1385894712005529)
| 2.4.1 | Hydrotalcite |
|---|---|
| Simultaneous removal of cationic and anionic heavy metal contaminants from electroplating effluent by hydrotalcite adsorbent with disulfide (S2-) intercalation | |
| Abstract Hydrotalcite materials are generally utilized for anionic pollutants due to its interlayered anion exchange ability. Their potentiality for cationic contaminants is rarely explored. In this study, disulfide ( S 2 - ) intercalated LDH material demonstrated capability to remove both heavy metal cations and oxyanions simultaneously from water. The S 2 - intercalation of LDH significantly improved its adsorption capability towards both heavy metal cations ( C o 2 + and N i 2 + ) and oxyanion ( C r O 4 2 - ). The adsorption amount of S-LDH towards C o 2 + and N i 2 + reached 88.6mg/g and 76.2mg/g, which are 405% and 281% higher than that of pristine LDH. For C r O 4 2 - removal, the adsorption amount reached 34.7mg/g, 402% higher than that of pristine LDH. The cations capture mechanism mainly depends on the novel layer sheet cation substitution mechanism based on irreversible precipitation and the generation of metal sulfide precipitates. Meanwhile, the interlayered S 2 - can be easily replaced by C r O 4 2 - to realize the simultaneous removal of both heavy metal cations and oxyanions. In the fixed-bed column experiments, 448 bed volume (BV) (672 mL) of simulating electroplating wastewater can be efficiently treated by yielding only 1 BV(15 mL) of chemical sludge, which is practically acceptable. This work provided a highly practical adsorption technology based on the S 2 - modification hydrotalcite material for the purification of heavy metal ions contaminated wastewater. | |
| 09/07/2019 00:00:00 | |
| Link to Article | |
2.5 Zero valent metal
Zerovalent iron (ZVI) is the most commonly used zerovalent metal (ZVM) for environmental remediation. ZVI is typically applied as a reductant and is capable of transforming (degrading) or sequestering a variety of contaminants found in groundwater and soil.[\[Source\]](https://www.enviro.wiki/index.php?title=Zerovalent_Iron_(ZVI)_(Chemical_Reduction_-_ISCR)#:\~:text=From%20Enviro%20Wiki,found%20in%20groundwater%20and%20soil.)
**Highlights:**
* Reducing the concentration of heavy metals including lead (Pb) and nickel (Ni) in organic contaminants such as municipal wastes and sewage sludge is of health and environmental importance. **Nanoscale zero-valent iron (NZVI) particles can effectively remove heavy metals from contaminated aqueous and solid media.** [\[Art. #ARTNUM\]](#article-96751-2744894627)
* **The hybrid zero-valent-iron (hZVI) process is a novel chemical treatment process that has shown promise for removing heavy metals and nutrients from industrial wastewaters.** In this study, a pilot-scale demonstration was conducted to continuously treat 3.8–7.6 L/min (1–2 gpm) of the flue-gas-desulfurization (FGD) wastewater at a coal-fired power plant for 5 months. \[...\] the process simultaneously removed a broad spectrum of heavy metals such as As(III), As(V), Cr(VI), Cd(II), Pb(II) and Cu(II) from mg/L to near or sub-ppb (μg/L) level after a single-stage treatment. The process consumed about 0.3 kg ZVI per 1 m 3 FGD wastewater treated at a cost of about US$0.6/m 3 . Solid waste production and energy consumption were reasonably low. The successful pilot study demonstrated that the hZVI technology can be a low-cost, high-performance treatment platform for solving some of the toughest heavy metal water problems.[ \[Art. #ARTNUM\]](#article-96751-2094605413)
* The present study investigated the reactivity and ability of permeable reactive barriers \[zero-valent iron (ZVI)-barrier plus biobarrier) to remove various contaminants (Cd, As, Zn, Cu, Mn, Cr, NO3 −, NH4 +, and CODcr) from synthetic leachate. Two different reactive materials were used in this study, namely ZVI and autoclaved lightweight concrete (ALC).[ \[Art. #ARTNUM\]](#article-96751-1990602760)
| 2.5.1 | Zero valent metal |
|---|---|
| Impregnation of Nano Zero-Valent Iron in Biomaterials for Remediation of Wastewater | |
| Nano zero-valent iron (nZVI) is widely used to remediate groundwater and wastewater from heavy metals and stable organic pollutants (Permeable Reactive Barriers). This is caused by the fact that Fe0 reduces several halogenous hydrocarbons, chlorine-containing pesticides, organic dyes, nitrozo compounds, explosives and others. The restoring ability is used for reduction of CrO4-2, Cr2O7-2, ClO4-, NO3- ions and elimination of Hg+2, Ni+2,Cd+2, Pb+2 as well as of a number of radionuclides from water. nZVIs had found wide application in the USA but in Europe this method appeared later. The cost of these methods for remediation of water depends on many factors (type of pollution, cost of reagents, the purpose and degree of remediation, remediation methods and other). That is why revealing of new reductants and methods for reduction of Fe+2 and Fe+3 up to Fe0 is an actual problem. The objective of the present research is impregnation of nZVL in bioorganic materials and obtaining of hybrid organic-inorganic reactive barriers. In this paper, we present preliminary results on the development of methods for impregnating of the nZVI in biopolymers. On the basis of these materials, it is possible to obtain cheap biosorbents with versatile properties able to simultaneously remove the heavy metals (including radio nuclides) and stable organic pollutants. Biopolymers contain many complex-forming functional groups, including hydroxyl, carboxyl, carbonyl, ether and other groups. These groups have the ability to stabilize the nanosize particles and prevent formation of large-size particles. Biosorbents have a high sorption capacity towards ions of heavy metals, which are higher than a similar capacity of inorganic sorbents. The matrix (biomaterial) plays a role of a sorbent of heavy metals and on the other hand the particles of impregnated iron are reactive barriers for toxic metal ions and stable organic pollutants. A method for activation of biomaterials (wood processing wastes, sawdust, shavings, chips, cereal crop residues) has been developed, which includes their hydrothermal treatment at 2000C at a pressure of 2,0-2,5 MPa(for 1 h) and then rapid reduction of pressure that leads to decomposition of the wood structure and increase of the surface. Immobilization of nZVI in biopolymers and in wood of some plants has been carried out by chemical method (by sodium borohydride) and by plant extracts. It was determined that the wood of some local plants is a reduction agent for iron compounds. The possibility of obtaining nZVI in wood present in its reducing agents gives us hope that it is possible to create a new type complex biosorbent by methods of "green chemistry" that excludes stages extraction of reductants from biomaterials. It is determined that with similar methods, it is possible to impregnate (apply) nZVI in porous inorganic compounds. Microstructure of sorbents has been studied by optical and electronic scanning microscopes (NIKON ECLIPSE LV 150, NMM-800TRF, NANOLAB-7). Sorbents have been analyzed by XRD method on the diffractometer DRON-3M (Cu-KI±, Ni filter, 2O/min). | |
| 03/16/2015 00:00:00 | |
| Link to Article | |
| 2.5.2 | Zero valent metal |
| Integration of nanoscale zero-valent iron and functional anaerobic bacteria for groundwater remediation: A review | |
| Abstract The technology of integrating nanoscale zero-valent iron (nZVI) and functional anaerobic bacteria has broad prospects for groundwater remediation. This review focuses on the interactions between nZVI and three kinds of functional anaerobic bacteria: organohalide-respiring bacteria (OHRB), sulfate reducing bacteria (SRB) and iron reducing bacteria (IRB), which are commonly used in the anaerobic bioremediation. The coupling effects of nZVI and the functional bacteria on the contaminant removal in the integrated system are summarized. Generally, nZVI could create a suitable living condition for the growth and activity of anaerobic bacteria. OHRB and SRB could synergistically degrade organic halides and remove heavy metals with nZVI, and IRB could reactive the passivated nZVI by reducing the iron (hydr)oxides on the surface of nZVI. Moreover, the roles of these anaerobic bacteria in contaminant removal coupling with nZVI and the degradation mechanisms are illustrated. In addition, this review also discusses the main factors influencing the removal efficiency of contaminants in the integrated treatment system, including nZVI species and dosage, inorganic ions, organic matters, pH, type of pollutants, temperature, and carbon/energy sources, etc. Among these factors, the nZVI species and dosage play a fundamental role due to the potential cytotoxicity of nZVI, which might exert a negative impact on the performance of this integrated system. Lastly, the future research needs are proposed to better understand this integrated technology and effectively apply it in groundwater remediation. | |
| 03/01/2019 00:00:00 | |
| Link to Article | |
| 2.5.3 | Zero valent metal |
| Method used for removing heavy metals in sludge with nano zero-valent iron, and special-purpose apparatus thereof | |
| The invention discloses a special-purpose apparatus used for removing heavy metals in sludge with nano zero-valent iron, and belongs to the field of environmental protection technology. The special-purpose apparatus comprises a first reactor and a second reactor; sludge obtained via pretreatment using the first reactor is delivered into the second reactor using a sludge pump; a stirrer is arranged in the middle part of the first reactor, and another stirrer is arranged in the middle part of the second reactor; an ultrasonic vibrator is arranged on the bottom of the first reactor; a magnet and a heavy metal recycling outlet are arranged on the bottom of the second reactor in a cooperative manner; and the second reactor is connected with a mud-water centrifugal separation device via another sludge pump. The invention also discloses a method used for removing heavy metals in sludge with nano zero-valent iron. In the special-purpose apparatus, pretreatment and reaction are carried out in the first reactor, and recycling is realized with an extracting agent. According to the method, ultrasonic wave is adopted in the reaction process, reaction time is shortened, treatment efficiency is increased, heavy metals in sludge are removed effectively, waste is changed into valuables, and development of environment protection and agriculture industry is promoted. | |
| 05/31/2017 00:00:00 | |
| Link to Article | |
| 2.5.4 | Zero valent metal |
| Pilot-scale demonstration of the hybrid zero-valent iron process for treating flue-gas-desulfurization wastewater: Part II | |
| The hybrid zero-valent-iron (hZVI) process is a novel chemical treatment process that has shown promise for removing heavy metals and nutrients from industrial wastewaters. In this study, a pilot-scale demonstration was conducted to continuously treat 3.8–7.6 L/min (1–2 gpm) of the flue-gas-desulfurization (FGD) wastewater at a coal-fired power plant for 5 months. In this paper, a spike test was conducted to evaluate performance of the hZVI process for removing selected toxic metals at artificially elevated concentrations. The results showed that a multiple-stage hZVI process could decrease selenate-Se from 22 mg/L to ∼10 μg/L and dissolved Hg 2+ from 1.15 mg/L to ∼10 ng/L. In addition, the process simultaneously removed a broad spectrum of heavy metals such as As(III), As(V), Cr(VI), Cd(II), Pb(II) and Cu(II) from mg/L to near or sub-ppb (μg/L) level after a single-stage treatment. The process consumed about 0.3 kg ZVI per 1 m 3 FGD wastewater treated at a cost of about US$0.6/m 3 . Solid waste production and energy consumption were reasonably low. The successful pilot study demonstrated that the hZVI technology can be a low-cost, high-performance treatment platform for solving some of the toughest heavy metal water problems. | |
| 11/01/2012 00:00:00 | |
| Link to Article | |
| 2.5.5 | Zero valent metal |
| Removal of mixed contaminants by Fe0-based biobarrier in flow-through columns using recycled waste materials | |
| The present study investigated the reactivity and ability of permeable reactive barriers [zero-valent iron (ZVI)-barrier plus biobarrier) to remove various contaminants (Cd, As, Zn, Cu, Mn, Cr, NO3 −, NH4 +, and CODcr) from synthetic leachate. Two different reactive materials were used in this study, namely ZVI and autoclaved lightweight concrete (ALC). After 90 days of column operation, the contaminant profiles were determined along the length of the columns. The heavy metals were extensively removed in the bio-ALC and sequential barriers (ZVI plus bio-ALC), however the removal efficiencies for the heavy metals Zn and Cr in the ALC and bio-ALC barriers were comparatively low. Nitrate was completely removed (>99.9%) in the ALC, bio-ALC, and sequential barriers. More than 50% of the produced ammonium and organic materials were removed in the biologically reactive zone of the sequential barriers. The results of the present study suggest that sequential barriers are one of the best solutions for in situ remediation and that they can be applied to clean up the leachate released from landfills. | |
| 09/01/2009 00:00:00 | |
| Link to Article | |
| 2.5.6 | Zero valent metal |
| Review of zero-valent aluminium based water and wastewater treatment methods | |
| Abstract Zero-valent metals (ZVM) are widely used to remove heavy metals, contaminants, toxicity, etc. from water and wastewater. Zero-valent aluminium (ZVAl) has large surface area and high surface reactivity. It has enormous flexibility for the in-situ application. ZVAl can be applied as either a single or a bimetallic system as well as advanced oxidation processes (AOPs). It is observed that ZVAl is capable of generating hydroxyl and sulfate radicals in water medium, which remove non-biodegradable pollutants from aqueous solution. ZVAl-based processes can remove non-biodegradable organic contaminants from water medium within a short duration. ZVAl is also used as a reducing agent. It is efficient to reduce toxic hexavalent chromium to less toxic trivalent chromium. ZVAl, in various combinations in bimetallic system (Fe/Al, Pd/Al, Cu/Al), is able to remove various contaminants from aqueous medium. Overall, it can be concluded that ZVAl-based methods for water and wastewater treatment are promising environmental technologies. | |
| 06/01/2018 00:00:00 | |
| Link to Article | |
| 2.5.7 | Zero valent metal |
| Selective removal of heavy metals from landfill leachate by reactive granular filters | |
| Abstract The pre-treatment of landfill leachate prior to its co-treatment in the municipal plants of waste water processing could represent an appropriate and cost-effective solution for its management. Pre-treatment is necessary especially to remove heavy metals, which may be transferred to the excess sludge preventing its valorisation. In the present paper, we propose a chemical-physical pre-treatment of leachate using four different granular reactive media able to selectively remove the contaminants present in the leachate. The efficiency of these materials was investigated using synthetic leachate through batch tests and a column test. In the latter case the four materials were placed in two columns connected in series and fed an under constant upward flow (0.5 mL/min). The first column was filled half (50 cm) with a granular mixture of zero valent iron (ZVI) and pumice and half (50 cm) with a granular mixture of ZVI and granular activated carbon (GAC). The second column, which was fed with the effluent of the first column, was filled half with zeolite (chabazite) and half with GAC. Heavy metals were mainly removed by the ZVI/pumice and ZVI/GAC steps with a removal efficiency that was higher than 98, 94 and 90% for copper, nickel and zinc, respectively, after 70 days of operation. Ammonium was removed by zeolite with a removal efficiency of 99% up to 23 days. The average reduction of the chemical oxygen demand (COD) was of 40% for 85 days, whereas chloride and sulphate removal was negligible. | |
| 12/01/2018 00:00:00 | |
| Link to Article | |
| 2.5.8 | Zero valent metal |
| Single-step removal of Hexavalent chromium and phenol using meso zerovalent iron. | |
| Abstarct Novel meso-zero valent iron (mZVI) was investigated for treating complex wastewater containing toxic heavy metal Cr6+ and organic compound phenol. This study is first of its kind illustrating coupled removal in single-step with H2O2 playing a major role as an oxidant and reductant. The mechanism involved was electron transfer from Fe0/2+ to Cr6+ resulting in Fe2+/3+ which in turn was consumed for phenol oxidation returning as Fe2+ into the system for further Cr6+ reduction. While comparing, single-step simultaneous removal of Cr6+ and phenol showed better performance in terms of pollutant removal, Fe2+/3+ recurrent reaction and precipitation generation, double-tep sequential removal performed better in iron active-corrosion time. It was also observed that the entire redox cycle of Cr6+-Cr3+-Cr6+ was reusable for co-contaminant phenol degradation at all pH with the recurrence of Fe2+-Fe3+-Fe2+. The proposed technique was checked for its viability in a single batch reactor and the complex chemistry of the reactions are unfolded by conducting chemical speciation and mass balance study at every stage of reaction. The unique functioning of mZVI was proven with micro-analysis of ZVI’s surface and compared with granular ZVI, cZVI. The results obtained from this study open the door for a safer and cleaner single treatment system in removing both toxic heavy metals and organic compounds from contaminated surface water, groundwater and many such industrial effluents. | |
| 06/01/2020 00:00:00 | |
| Link to Article | |
| 2.5.9 | Zero valent metal |
| The removal of lead and nickel from the composted municipal waste and sewage sludge using nanoscale zero-valent iron fixed on quartz | |
| Abstract Reducing the concentration of heavy metals including lead (Pb) and nickel (Ni) in organic contaminants such as municipal wastes and sewage sludge is of health and environmental importance. Nanoscale zero-valent iron (NZVI) particles can effectively remove heavy metals from contaminated aqueous and solid media. It was accordingly hypothesized that it is possible to recycle and detoxify organic waste materials containing heavy metals using NZVI and NZVI fixed on quartz (QNZVI). The objective was to investigate the effects of NZVI type, concentration (2% and 5%) and contact time on the removal of Pb and Ni from raw compost, compost fermented with beet molasses, and leachate using a factorial design. The results indicated the significant reduction of DTPA- Pb and DTPA-Ni concentration, in all the organic compounds treated with NZVI and QNZVI (P= 0.01), compared with control. Increased concentration of NZVI in all treatments, increased the rate of DTPA-Pb and DTPA-Ni (P= 0.01) at 113.1% and 180% for Pb (NZVI at 2% and 5%), and at 16.3% and 23.3% for Ni, irrespective of the NZVI type. The reducing trend of extractable Pb and Ni in all the organic compounds was the same, quick reduction at the beginning, followed by a negligible rate. The highest reduction rates for Pb (at one hour) and Ni (at 672 h) were equal to 72.93% and 23.27%, respectively. NZVI at 2% was more efficient than NZVI at 5%. There were not any significant differences between NZVI and QNZVI on the removal of Pb and Ni from the organic contaminants. It is possible to immobilize and reduce the concentration of heavy metals such as Pb and Ni in organic contaminants using NZVI, which is affected by NZVI properties, concentration, and contact time, as well as by organic contaminant type. | |
| 11/01/2017 00:00:00 | |
| Link to Article | |
2.6 Nanomaterials
Nanomaterials are chemical substances or materials that are manufactured and used at a very small scale. Nanomaterials are developed to exhibit novel characteristics compared to the same material without nanoscale features, such as increased strength, chemical reactivity or conductivity. [\[Source\]](http://www.safenano.org/knowledgebase/resources/faqs/what-is-a-nanomaterial/#:\~:text=Nanomaterials%20are%20chemical%20substances%20or,strength%2C%20chemical%20reactivity%20or%20conductivity.)
Commonly researched nanomaterials in waste remediation are nanoscale zero valent iron, carbon nanotubes, nanoparticles etc.
**Highlights:**
* In this work, novel nanomaterials, including **carbon-based nanomaterials, zero-valent metal, metal-oxide based nanomaterials, and nanocomposites, and their applications for the removal of heavy metal ions from wastewater were systematically reviewed.** Their efficiency, limitations, and advantages were compared and discussed. Furthermore, the promising perspective of nanomaterials in environmental applications was also discussed and potential directions for future work were suggested.[ \[Art. #ARTNUM\]](#article-96119-2921291027)
* **The treatment columns for phosphorus sorption consisted of two 2.54 cm diameter PVC columns containing porous ceramic media nano coated with iron formed into a monolith**, manufactured by MetaMateria Technologies, LLC, Columbus, Ohio. The denitrification columns were 5.1 cm diameter PVC buckets containing loosely packed porous ceramic media (manufactured from MetaMateria) crushed to have a diameter of roughly 1 cm. Results showed that the phosphorus media effectively removed phosphorus from simulated tile drain water from 0.12 mg/L-P to undetectable levels. Initially, denitrification did not occur and was not encouraged by the additional of a microbial inoculum. However, once ethanol was added to increase the carbon to nitrogen ratio, treatment was very effective. The nitrate was reduced from 83 mg/L-N to 0.6 mg/L-N. [\[Art. #ARTNUM\]](#article-96119-2755455545)
* This work highlights up-to-date methods for the removal of heavy metals from water using the technique of adsorption. After a comprehensive review of the range of materials used as adsorbents to remove heavy metals, the paper focuses on one particular technique, involving **carbon nanotubes (CNTs)**. This study shows that using deep eutectic solvents (DESs) as a functionalization agent to replace ionic liquids (ILs) has a number of advantages, including lower costs, easier availability of materials and environmentally friendliness. In sum, it suggests that the most efficient adsorption process is to use functionalized CNTs with DESs as an adsorbent. The critical analysis and conclusions emerging from this study should be of benefit to engineers, environmental scientists and chemists interested in the use of carbon nanotubes for use in environmental remediation. [\[Art. #ARTNUM\]](#article-96119-2945202622)
| 2.6.1 | Nanomaterials |
|---|---|
| Eliminating Heavy Metals from Water with Nano-Sheet Minerals as Adsorbents | |
| Heavy metals usually referred to those with atomic weights ranging from 63.5 to 200.6. Because of natural-mineral dissolution and human activities such as mining, pesticides, fertilizer, metal planting and batteries manufacture, etc., these heavy metals, including zinc, copper, mercury, lead, cadmium and chromium have been excessively released into water courses, like underground water, lake and river, etc. The ingestion of the heavy metals-contaminated water would raise serious health problems to human beings even at a low concentration. For instance, lead can bring human beings about barrier to the normal function of kidney, liver and reproductive system, while zinc can cause stomach cramps, skin irritations, vomiting and anemia. Mercury is a horrible neurotoxin that may result in damages to the central nervous system, dysfunction of pulmonary and kidney, chest and dyspnea. Chromium (VI) has been proved can cause many diseases ranging from general skin irritation to severe lung carcinoma. Accordingly, the World Health Organization announced the maximum contaminant levels (MCL) for the heavy metals in drinking water. There are numerous processes for eliminating heavy metals from water in order to provide citizens safe drinking water, including precipitation, adsorption, ion exchange, membrane separation and biological treatment, etc. Adsorption is considered as a potential process for deeply removing heavy metals, in which the selection of adsorbents plays a predominant role. Nano-sheet minerals as the adsorbents are currently the hottest researches in the field. They are obtained from layered minerals, such as montmorillonite, graphite and molybdenite, through the processing of intercalation, electrochemical and mechanical exfoliation, etc. Nano-sheet minerals are featured by their large specific surface area, relatively low costs and active adsorbing sites, leading to be effective and potential adsorbents for heavy metals removal from water. Montmorillonite was usually pre-interacted with organics to increase the interlayer space, and then exfoliated to single or several layers by ultraphonic. Among the nano-sheets, the surfaces are strongly charged negatively, while the edges are positively charged. This characteristic allows the adsorption of cations or anions, as well as the substances with negative or positive charges. Graphite can be oxidized and exfoliated into graphene oxide (GO), which has a huge specific surface area and plentiful of functional groups such as carboxyl, epoxy, carbonyl and hydroxyl, leading to high adsorption capacity to heavy metals in water. Nano-sheet molybdenite is a novel two-dimensional material with single or several layers of MoS2 sheets. The most common method to prepare nano-sheet molybdenite is exfoliated from bulk molybdenite through chemical method based on ion intercalation process. A large quantity of functional groups and S atom on the sheets are the active sites for adsorbing heavy metals in water. Nano-sheet minerals are used as adsorbents in the form of three-dimension hydrogels. They are featured by the huge specific surface area and high adsorption efficiency. In addition, the clean and smooth surfaces allow heavy metals to adsorb directly by film dispersion. Without any barrier of mesopores and micropores, the adsorption rate could be well improved. These characteristics would lead to the extremely large adsorption capacity and high adsorption rate. Currently, nano-sheet minerals as adsorbent is a very hot research topic in the field of heavy metal removal. It is expected that nano-sheet minerals will be promising adsorbents in the removal of heavy metals from water. | |
| 12/30/2017 00:00:00 | |
| Link to Article | |
| 2.6.2 | Nanomaterials |
| Nanocellulose: Extraction and application as a sustainable material for wastewater purification | |
| Abstract With the increase in water quality regulations and decrease in available fresh water supplies, scientists around the world are focusing on renewable raw materials and environmentally friendly, cost-effective materials for water purification. Among these, nanocellulose has gained considerable interest because of its excellent properties. Many laboratory operations depend on the filtration process that is performed with cellulose-based filter papers. Nanocellulose's inherent fibrous nature and remarkable mechanical properties, including low cost and bio-compatibility make nanocellulose a huge potential component in water filtration membranes. Nanocellulose is a very promising adsorbent for removing heavy metals, viruses, dyes, etc. due to its high surface area-to-volume ratio, low cost, high natural abundance, and inherent environmental inertness. Moreover, the surface of nanocellulose has easily functionalizable OH groups, and this facilitates the incorporation of chemical moieties that may increase the binding efficiency of pollutants to the nanocellulosic materials. The materials based on cellulose and its derivatives have been used for more than 150 years in a wide variety of applications, such as food, paper production, biomaterials, and pharmaceuticals. In recent years, nanotechnologies have been promoted as having great potential for reducing costs and developing efficiency in pollution prevention, treatment, and clean up. Two applications for cellulose nanomaterials in this area that have achieved interest are as an active sorbent material for contaminants and as a stabilizer for other active particles. Cellulose nanofibers (CNF) are one of the types of cellulose nanomaterials. CNFs are a promising substitute adsorbent due to their high surface area to-volume ratio, low cost, high natural abundance, and inherent environmental inertness. Furthermore, CNFs readily functionalized surface facilitates the incorporation of chemical moieties that may enhance the binding efficiency of pollutants to the CNF. | |
| 01/01/2018 00:00:00 | |
| Link to Article | |
| 2.6.3 | Nanomaterials |
| Nanomaterials for the Removal of Heavy Metals from Wastewater | |
| Removal of contaminants in wastewater, such as heavy metals, has become a severe problem in the world. Numerous technologies have been developed to deal with this problem. As an emerging technology, nanotechnology has been gaining increasing interest and many nanomaterials have been developed to remove heavy metals from polluted water, due to their excellent features resulting from the nanometer effect. In this work, novel nanomaterials, including carbon-based nanomaterials, zero-valent metal, metal-oxide based nanomaterials, and nanocomposites, and their applications for the removal of heavy metal ions from wastewater were systematically reviewed. Their efficiency, limitations, and advantages were compared and discussed. Furthermore, the promising perspective of nanomaterials in environmental applications was also discussed and potential directions for future work were suggested. | |
| 03/12/2019 00:00:00 | |
| Link to Article | |
| 2.6.4 | Nanomaterials |
| Removal of Nutrients from Agricultural Drainage Water using Nano-Engineered Porous Ceramic Media | |
| Abstract. Drainage practices that enable surface and subsurface agricultural water management to increase crop productivity may increase the transport of nutrients to receiving waters. Residual phosphorus and nitrogen can leach from the soil profile by subsurface water movement and be carried into surface water through tiles. This research examined nutrient removal from agricultural drainage water using microbial nitrification/denitrification and phosphorus sorption. To simulate agricultural drainage water, 208 L drums were filled with a loamy soil, slurry manure was applied to the surface, water was added to simulate rainfall, and effluent, was collected from the bottom of the drums. The treatment columns for phosphorus sorption consisted of two 2.54 cm diameter PVC columns containing porous ceramic media nano coated with iron formed into a monolith, manufactured by MetaMateria Technologies, LLC, Columbus, Ohio. The denitrification columns were 5.1 cm diameter PVC buckets containing loosely packed porous ceramic media (manufactured from MetaMateria) crushed to have a diameter of roughly 1 cm. Results showed that the phosphorus media effectively removed phosphorus from simulated tile drain water from 0.12 mg/L-P to undetectable levels. Initially, denitrification did not occur and was not encouraged by the additional of a microbial inoculum. However, once ethanol was added to increase the carbon to nitrogen ratio, treatment was very effective. The nitrate was reduced from 83 mg/L-N to 0.6 mg/L-N. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 2.6.5 | Nanomaterials |
| Review on heavy metal adsorption processes by carbon nanotubes | |
| Abstract The most important and indispensable substance for life on earth is water. Regrettably, the growths of civilization, population, and industrssialization have led to a steady deterioration in the quality of available water resources. Heavy metals are a particular problem because of their high toxicity. This work highlights up-to-date methods for the removal of heavy metals from water using the technique of adsorption. After a comprehensive review of the range of materials used as adsorbents to remove heavy metals, the paper focuses on one particular technique, involving carbon nanotubes (CNTs). Tests have confirmed that CNTs are highly efficient, but have also revealed some drawbacks. Further adjustments and refinements are therefore required to improve their ability to remove heavy metals. This study shows that using deep eutectic solvents (DESs) as a functionalization agent to replace ionic liquids (ILs) has a number of advantages, including lower costs, easier availability of materials and environmentally friendliness. In sum, it suggests that the most efficient adsorption process is to use functionalized CNTs with DESs as an adsorbent. The critical analysis and conclusions emerging from this study should be of benefit to engineers, environmental scientists and chemists interested in the use of carbon nanotubes for use in environmental remediation. | |
| 09/01/2019 00:00:00 | |
| Link to Article | |
2.7 Sludge (particles)
Sludge particles, such as (dry) activated sludge and alum sludge can be used to remediate waste streams from heavy metals and some minerals..
**Highlights:**
* A wide range of batch experiments were carried out for estimation of the key process parameters in competitive biosorption of Pb 2+ , Hg 2+ , Cr 3+ and As 5+ from simulated of wastewater onto **dry activated sludge** in batch adsorber. [ \[Art. #ARTNUM\]](#article-96098-2008237009)
* This study attempts to determine effectiveness of **dried alum sludge as media to remove phosphorus from different kind of water samples.** Three types of wastewater were selected; synthetic phosphate solution, wastewater and river water. The continuous flow test approach with constant hydraulic loading is used in this study. The results indicate that dried alum sludge from water treatment plant has great potential as to remove the phosphate from synthetic water, river water and wastewater. [\[Art. #ARTNUM\]](#article-96098-1822564579)
| 2.7.1 | Sludge (particles) |
|---|---|
| Aerobic granular sludge technology: Mechanisms of granulation and biotechnological applications | |
| Abstract Aerobic granular sludge (AGS) is a novel microbial community which allows simultaneous removal of carbon, nitrogen, phosphorus and other pollutants in a single sludge system. AGS is distinct from activated sludge in physical, chemical and microbiological properties and offers compact and cost-effective treatment for removing oxidized and reduced contaminants from wastewater. AGS sequencing batch reactors have shown their utility in the treatment of abattoir, live-stock, rubber, landfill leachate, dairy, brewery, textile and other effluents. AGS is extensively researched for wide-spread implementation in sewage treatment plants. However, formation of AGS takes relatively much longer time while treating low-strength wastewaters like sewage. Strategies like increased volumetric flow by means of short cycles and mixing of sewage with industrial wastewaters can promote AGS formation while treating low-strength sewage. This article reviewed the state of research on AGS formation mechanisms, bioremediation capabilities and biotechnological applications of AGS technology in domestic and industrial wastewater treatment. | |
| 01/01/2018 00:00:00 | |
| Link to Article | |
| 2.7.2 | Sludge (particles) |
| CHLORIDE REMOVAL FROM LANDFILL LEACHATE BY THE ULTRA-HIGH LIME WITH ALUMINUM PROCESS | |
| Besides organic contaminants, nutrients and heavy metals, high concentrations of chloride have also been observed in landfills accepting ash deposition from waste-to-energy applications, which is difficult be removed in wastewater treatment processes. Chloride may percolate and cause surface salt formation and soil alkalinity increase, thereby resulting in loss of soil. In plants, chloride tends to accumulate in the tissues, especially the leaves. Conventional removal techniques are not feasible from the cost perspective. In this research, the ultra-high lime with aluminum process was evaluated for chloride removal from landfill leachate by precipitation as calcium chloroaluminate (Ca4Al2Cl2(OH)12) in the presence of calcium and aluminum at high pH. Chloride removal was found to be a function of both aluminum concentration and pH. Chloride removal increased with the increase of alum addition until 20 mg/L, after which the chloride removal became moderate. With the increase of pH, obviously more chloride was removed. At pH of 10, the removal reached 90%. To save the chemical costs, alum sludge from a drinking water treatment plant was tested for the removal of chloride from the landfill leachate. The results showed that the supernatant of the alum sludge was more efficient than that of alum sludge suspension in chloride removal. The usage of alum sludge can dramatically save the chemical costs. | |
| 05/21/2017 00:00:00 | |
| Link to Article | |
| 2.7.3 | Sludge (particles) |
| Competitive Biosorption of Lead Mercury Chromium and Arsenic Ions onto Activated Sludge in Batch Adsorber | |
| A wide range of batch experiments were carried out for estimation of the key process parameters in competitive biosorption of Pb 2+ , Hg 2+ , Cr 3+ and As 5+ from simulated of wastewater onto dry activated sludge in batch adsorber. Eleven isotherm models were used for single component and five models for multi-component systems. The Langmuir model gave the best fit for the data of single component, while the binary, ternary and quaternary systems were fitted successfully with extended Langmuir model. The biosorption capacity for single metal decreased by 11-51 %, 53-88 % and 79-94 % in the binary, ternary and quaternary systems respectively at the optimum agitation speed 600-800 rpm. An order of metal biosorption capacity onto dried activated sludge was the same in the case of competitive multi-metal sorption conditions as it was for single-element sorption, namely Pb 2+ > Cr 3+ > Hg 2+ > As 5+ . FT-IR analysis was carried out before and after biosorption to determine which functional groups were responsible for binding the heavy metals. Kinetic study showed that pseudo- second order model was well fitted for all metals ions. R 2 used to enhance the justification analysis for each used model. | |
| 10/16/2012 00:00:00 | |
| Link to Article | |
| 2.7.4 | Sludge (particles) |
| Environmental impacts and cost-effectiveness of Thailand's centralized municipal wastewater treatment plants with different nutrient removal processes | |
| Abstract This research investigates the organic and nutrient removal efficiency of eight centralized municipal wastewater treatment plants (WWTP) in Thailand's capital Bangkok, under five treatment schemes. The environmental impacts were assessed using life cycle assessment, and the cost-effectiveness was determined by life cycle cost assessment. The five treatment schemes were contact stabilization (scheme A/base case), activated-sludge with nutrient removal (scheme B), cyclic activated-sludge (scheme C), two-stage activated-sludge (scheme D), and vertical loop reactor activated-sludge (scheme E). The results showed that scheme A achieved the highest organic removal efficiency (93.01% on average), with all other treatment schemes achieving more than 83% removal efficiency. Scheme E achieved the highest total phosphorus and total nitrogen removal efficiencies (69.12% and 59.74% on average), and scheme C was effective in removing total Kjeldahl nitrogen and ammonia (82.84% and 89.12% on average). The environmental impact assessment indicated that electricity use was the major contributor of almost all environmental impact categories except aquatic eutrophication. Scheme E had the lowest environmental impacts in almost all categories except aquatic eutrophication. Total costs (including operation, maintenance, and environmental costs) of WWTPs with nutrient removal were lower than without nutrient removal. Scheme E had the lowest total cost (2.754 THB2017 per m3) and lowest compounds removal costs, in addition to highest nutrient removal efficiency. Scheme E is the most cost-effective scheme with lowest environmental impacts (i.e., the most eco-efficiency scheme). | |
| 05/01/2020 00:00:00 | |
| Link to Article | |
| 2.7.5 | Sludge (particles) |
| Influence of Contact Time on Effectiveness of Recycle Alum Sludge as Pollutant Removal | |
| Presence of phosphorus in agriculture and other activities near the water bodies, lead to algae growth and other aquatic plants in a pond. Alum sludge can be converted into solid waste material and is useful application as low cost effectiveness removal in wastewater treatment facilities. This finding focuses on an innovation approach to treat the wastewater from low-cost adsorption material and promoting the green technology for the preservation of environment. This study attempts to determine effectiveness of dried alum sludge as media to remove phosphorus from different kind of water sample. Three types of wastewater were selected; synthetic phosphate solution, wastewater and river water. The continuous flow test approach with constant hydraulic loading is used in this study. Two condition of alum sludge height was employed i.e 12 cm and 24 cm. Alum sludge was grind and sieved through 2.36 mm sieve size in dry condition. The initial phosphate concentration was set for 2.6 mg/L. Concentration PO 4 sample from river and wastewater plant were 1.66 mg/L and 2.78 mg/L respectively. Test was monitored over 700 hours or 30 days with constant flow rate. The results indicated that different removal rate obtained from different height of alum sludge. The maximum percentage removal ranges from 70 % to 95 %. The results indicate that dried alum sludge from water treatment plant has great potential as to remove the phosphate from synthetic water, river water and wastewater. | |
| 07/07/2015 00:00:00 | |
| Link to Article | |
2.8 Biopolymers
Biopolymers are industrially attractive because they are, capable of lowering transition metal ion concentrations to sub-part per billion concentrations, widely available, and environmentally safe. Another attractive feature of biopolymers is that they possess a number of different functional groups, such as hydroxyls and amines, which increase the efficiency of metal ion uptake and the maximum chemical loading possibility. New polysaccharide-based-materials were described as modified biopolymer adsorbents (derived from chitin, chitosan, and starch) for the removal of heavy metals from the wastewater.[\[Paper\]](https://www.sciencedirect.com/science/article/pii/S1878535210001334#s0030)
**Highlights:**
* Many biopolymer materials which are capable of adsorbing have been developed as modified materials and applied for the removal of heavy metals from metal-contaminated wastewater, especially modified natural rubber, modified Lyocell fiber, and chitosan-based adsorbents. Moreover, chitosan derivatives such as chitosan-containing nitrogen, phosphorus, sulfur, and ethers have been studied as adsorbents as well. [\[Paper\]](https://link.springer.com/article/10.1007%2Fs00253-016-7646-x)
* Keratin protein fiber (AKF TM ) is a renewable source of biosorbent that can be used for filtration of heavy metal and nanosize contaminants. The major composition of keratin fiber is the structured protein micofibril, consisting of numerous nanosized pores. The combination of nanostructure and metal binding capacity protein sites make it an ideal material for removal of heavy metals from solutions.[ \[Art. #ARTNUM\]](#article-96323-2036889827)
* In this study, the preparation, characterization and heavy metal removal ability of chitosan–ethyl acrylate (CEA) biopolymer were investigated. Ethyl acrylate was successfully grafted to chitosan, which was characterized by Fourier transform infrared spectroscopy (FTIR) and nuclear magnetic resonance (NMR). Three heavy metal cations (Pb 2+ , Cd 2+ and Zn 2+ ) were removed from the simulated wastewater in batch mode, and the effect of initial metal ions concentration, adsorbent dosage, solution temperature, contact time and initial pH on the adsorption efficiency was illustrated. The maximum Pb 2+ , Cd 2+ and Zn 2+ removal efficiency of 92%, 86% and 98% were achieved, respectively.[ \[Art. #ARTNUM\]](#article-96323-2015768761)
* Heavy metal pollution has raised a lot of concerns because of its bioaccumulation and non-degradability. A variety of methods have been applied in removal of heavy metals. This paper focused on the method of biosorption using biopolymer-based adsorbents in removing heavy metals from waster water. **Cellulose and chitin/chitosan are abundant in supply and contain reactive functional groups.** Cellulose-based adsorbents prepared from direct chemical modification or graft copolymerization are proved to show chelating ability to bind heavy metals. Chitin-and chitosan-based adsorbents have improved mechanical strength and better resistance to chemical conditions after physical or chemical modification. The regeneration and reusability of biopolymer-based adsorbents were also discussed in this paper.[ \[Art. #ARTNUM\]](#article-96323-2012650961)
| 2.8.1 | Biopolymers |
|---|---|
| Application of Biopolymer-Based Adsorbents in Removal of Heavy Metals | |
| Heavy metal pollution has raised a lot of concerns because of its bioaccumulation and non-degradability. A variety of methods have been applied in removal of heavy metals. This paper focused on the method of biosorption using biopolymer-based adsorbents in removing heavy metals from waster water. Cellulose and chitin/chitosan are abundant in supply and contain reactive functional groups. Cellulose-based adsorbents prepared from direct chemical modification or graft copolymerization are proved to show chelating ability to bind heavy metals. Chitin-and chitosan-based adsorbents have improved mechanical strength and better resistance to chemical conditions after physical or chemical modification. The regeneration and reusability of biopolymer-based adsorbents were also discussed in this paper. | |
| 10/01/2014 00:00:00 | |
| Link to Article | |
| 2.8.2 | Biopolymers |
| Degradation characteristic of TiO2-chitosan adsorbent on Rhodamine B and purification of industrial wastewater | |
| Based on biosorption and photodegradation coupling technology, a novel adsorbent, which not only adsorbs the heavy metal ions but also degrades organic compound, was prepared by immobilization of nano-TiO2 on chitosan matrix. Degradation characteristic of Rhodamine B (Rh.B) was investigated by TiO2-chitosan adsorbents. The results showed that degradation ratio reached 94.3% by 0.2 g adsorbents under ultraviolet radiation light (UV) at initial Rh.B concentration of 10 mg/L and optimal pH of 9.0. Degradation and adsorption behavior characteristics were discussed in the presence of binary pollutants (Rh.B and Ag+). The coexistence of Ag+ intensely inhibited the degradation ability of Rh.B. Higher Ag+ concentration weakened the degradation ability. However, Rh.B did not affect the adsorption capacity of Ag+. Moreover, TiO2-chitosan adsorbent contributed to a higher degradation ability of organic pollutants in practical wastewater. Degradation capacity of contaminants in paper-making wastewater reached 60.8 mg/g at the initial COD concentration of 2,000 mg/L. | |
| 05/01/2011 00:00:00 | |
| Link to Article | |
| 2.8.3 | Biopolymers |
| Ethyl acrylate grafted chitosan for heavy metal removal from wastewater: Equilibrium, kinetic and thermodynamic studies | |
| Abstract In this study, the preparation, characterization and heavy metal removal ability of chitosan–ethyl acrylate (CEA) biopolymer were investigated. Ethyl acrylate was successfully grafted to chitosan, which was characterized by Fourier transform infrared spectroscopy (FTIR) and nuclear magnetic resonance (NMR). Three heavy metal cations (Pb 2+ , Cd 2+ and Zn 2+ ) were removed from the simulated wastewater in batch mode, and the effect of initial metal ions concentration, adsorbent dosage, solution temperature, contact time and initial pH on the adsorption efficiency was illustrated. The maximum Pb 2+ , Cd 2+ and Zn 2+ removal efficiency of 92%, 86% and 98% were achieved, respectively. The biosorption isotherm, kinetic, and thermodynamic parameters were also studied. The isotherm and kinetic data followed the Langmuir and pseudo-second-order models, respectively. The thermodynamic data showed that the biosorption process was a spontaneous, endothermic, and physisorption reaction. Efficient desorption of metal ions from the loaded CEA was found to be 98%, using HCl (0.6 M) at contact time of 80 min. The results indicated that CEA could be employed as a promising biopolymer for the removal of heavy metal from effluents. | |
| 06/01/2015 00:00:00 | |
| Link to Article | |
| 2.8.4 | Biopolymers |
| Keratin Protein Nano-fiber for Removal of Heavy Metals and Contaminants | |
| ABSTRACT Keratin protein fiber (AKF TM ) is a renewable source of biosorbent that can be used for filtration of heavy metal and nanosize contaminants. The major composition of keratin fiber is the structured protein micofibril, consisting of numerous nanosized pores. The combination of nanostructure and metal binding capacity protein sites make it an ideal material for removal of heavy metals from solutions. The mechanism of heavy metal uptake onto keratin protein involves a combination of several steps such as adsorption, precipitation, and ion exchange. Keratin protein has good tensile strength and is stable over a wide pH range. INTRODUCTION & BACKGROUND Conventional methods for removing heavy metals from contaminated solutions include chemical precipitation, carbon adsorption, membrane separation, microfiltration and the use of ion exchange resins. Many of the existing technologies for the removal of heavy metals from wastewaters are unable to achieve the low final concentrations required by new regulations. Furthermore, many existing treatment processes merely convert aqueous metal ions into solid sludges, which require costly landfill disposal. Biosorption, a relatively simple metal adsorption process, can meet the progressively stricter environmental discharge criteria. The term "biosorption" is used to describe the accumulation of metal ions by adsorption and/or ion exchange from solutions by materials of biological origin, particularly microorganisms, plant biomass and animal cells and extracts [1]. Thus the potential use of materials of biological origin in the treatment of heavy metal-contaminated wastewaters is of special importance. Organisms such as algae, bacteria, fungi, and yeasts have proved to be potential metal sorbents [1] | |
| 01/01/2001 00:00:00 | |
| Link to Article | |
2.9 Hydrogels
Hydrogels, which are crosslinked hydrophilic polymers, are capable of expanding their volumes due to their high swelling in water. Accordingly they are widely used in the purification of wastewater. Various hydrogels were synthesized and their adsorption behavior for heavy metals was investigated. The removal is basically governed by the water diffusion into the hydrogel, carrying the heavy metals inside especially in the absence of strongly binding sites.[\[Paper\]](https://www.sciencedirect.com/science/article/pii/S1878535210001334#s0030)
**Highlights:**
* heavy metal ions are removed effectively by forming hydrogen and chelating bonds with excess hydroxyl groups in the hydrogel.[ \[Art. #ARTNUM\]](#article-96696-3005157882)
* In this study, a polyampholyte hydrogel was well designed and prepared via a simple radical polymerization procedure. Due to the remarkable mechanical strength, the three-dimensional polyampholyte hydrogel could be fast separated, easily regenerated and highly reused. The sorption capacities were as high as 216.1 mg/g for Pb(II) and 153.8 mg/g for Cd(II) owing to the existence of the large number of active groups. The adsorption could be conducted in a wide pH range of 3–6 and the equilibrium fast reached in 30 min due to its excellent water penetration for highly accessible to metal ions. The fixed-bed column sorption results indicated that the polyampholyte hydrogel was particularly effective in removing Pb(II) and Cd(II) from actual industrial effluent to meet the regulatory requirements.[ \[Art. #ARTNUM\]](#article-96696-2183368156)
| 2.9.1 | Hydrogels |
|---|---|
| A highly efficient polyampholyte hydrogel sorbent based fixed-bed process for heavy metal removal in actual industrial effluent | |
| Abstract High sorption capacity, high sorption rate, and fast separation and regeneration for qualified sorbents used in removing heavy metals from wastewater are urgently needed. In this study, a polyampholyte hydrogel was well designed and prepared via a simple radical polymerization procedure. Due to the remarkable mechanical strength, the three-dimensional polyampholyte hydrogel could be fast separated, easily regenerated and highly reused. The sorption capacities were as high as 216.1 mg/g for Pb(II) and 153.8 mg/g for Cd(II) owing to the existence of the large number of active groups. The adsorption could be conducted in a wide pH range of 3–6 and the equilibrium fast reached in 30 min due to its excellent water penetration for highly accessible to metal ions. The fixed-bed column sorption results indicated that the polyampholyte hydrogel was particularly effective in removing Pb(II) and Cd(II) from actual industrial effluent to meet the regulatory requirements. The treatment volumes of actual smelting effluent using one fixed bed column were as high as 684 bed volumes (BV) (7736 mL) for Pb(II) and 200 BV (2262 mL) for Cd(II). Furthermore, the treatment volumes of actual smelting effluent using tandem three columns reached 924 BV (31,351 mL) for Pb(II) and 250 BV (8483 mL) for Cd(II), producing only 4 BV (136 mL) eluent. Compared with the traditional high density slurry (HDS) process with large amount of sludge, the proposed process would be expected to produce only a small amount of sludge. When the treatment volume was controlled below 209.3 BV (7103 mL), all metal ions in the actual industrial effluent could be effectively removed ( | |
| 02/01/2016 00:00:00 | |
| Link to Article | |
| 2.9.2 | Hydrogels |
| Biomass‐Derived Hybrid Hydrogel Evaporators for Cost‐Effective Solar Water Purification | |
| Solar vapor generation has presented great potential for wastewater treatment and seawater desalination with high energy conversion and utilization efficiency. However, technology gaps still exist for achieving a fast evaporation rate and high quality of water combined with low-cost deployment to provide a sustainable solar-driven water purification system. In this study, a naturally abundant biomass, konjac glucomannan, together with simple-to-fabricate iron-based metal-organic framework-derived photothermal nanoparticles is introduced into the polyvinyl alcohol networks, building hybrid hydrogel evaporators in a cost-effective fashion ($14.9 m(-2) of total materials cost). With advantageous features of adequate water transport, effective water activation, and anti-salt-fouling function, the hybrid hydrogel evaporators achieve a high evaporation rate under one sun (1 kW m(-2) ) at 3.2 kg m(-2) h(-1) out of wastewater with wide degrees of acidity and alkalinity (pH 2-14) and high-salinity seawater (up to 330 g kg(-1) ). More notably, heavy metal ions are removed effectively by forming hydrogen and chelating bonds with excess hydroxyl groups in the hydrogel. It is anticipated that this study offers new possibilities for a deployable, cost-effective solar water purification system with assured water quality, especially for economically stressed communities. | |
| 02/05/2020 00:00:00 | |
| Link to Article | |
2.10 biochar
Biochar is charcoal used as a soil amendment for both carbon sequestration and soil health benefits. Biochar is a stable solid, rich in carbon, and can endure in soil for thousands of years. Like most charcoal, biochar is made from biomass via pyrolysis. [\[Wiki\]](https://en.wikipedia.org/wiki/Biochar)
**Highlights:**
* In this study, a redox precipitation method was used to load manganese dioxide (MnO2) nanoparticles on biochar (BC) (BC@MnO2) pyrolyzed from the invasive water hyacinth, and the adsorption of Cd(II),Cu(II), Zn(II), and Pb(II) was investigated. \[...\] This study could lay an essential foundation to develop a win-win strategy for heavy metal ions removal from wastewater using biochar derived from water hyacinth. [\[Art. #ARTNUM\]](#article-96085-3015508606)
* The physicochemical properties and adsorption capacities of yak manure biochar (SP350-YMB) and modified yak manure biochar by H2O2 (AC-YMB) were investigated. Compared to SP350-YMB, the adsorption capacities of heavy metal ions (Pb2+, Cu2+, Cd2+ and Zn2+) were enhanced by AC-YMB in single-metal and multi-metal solutions. H2O2 modification reduced ash content and increased carboxyl content resulting in the major mechanism of heavy metal sorption shifting from precipitation with carbonate/phosphate to complexation with carboxyl. **Results from this study indicated that H2O2 modified biochar could act as effective surface sorbent to remove heavy metals, but its ability to remove multi-metal ions needs to be carefully evaluated on an individual basis.** [\[Paper\]](https://www.sciencedirect.com/science/article/pii/S0048969718305278)
| 2.10.1 | biochar |
|---|---|
| A critical review of clay-based composites with enhanced adsorption performance for metal and organic pollutants | |
| Abstract Adsorption techniques offer unique advantages owing to the use of synthetic (e.g., nanosized metal oxides and polymer-functionalized nanocomposites) and natural (e.g., clay and biochar) materials for pollutant removal. Although the most widely used adsorbent is activated carbon, extensive studies have highlighted the promising potential of modified clay minerals and biochar for removing heavy metal and organic pollutants from industrial, drinking, and eutrophic wastewater, due to their low cost and easy accessibility. However, clay modification using acids, calcination, polymers, or surfactants exhibits relatively low absorption/regeneration ability towards antibiotics, aromatics, and various dyes. The coexistence of numerous contaminants in industrial wastewater inhibited the performance of adsorbents, which accelerated the development of novel modified clay composites such as clay-biochar, organo-bentonite/sodium alginate beads, and enhanced biochar. This review summarizes recent studies and absorption mechanisms concerning clay composites based on various modification methods and component materials. The comparison of clay composites used for the removal of organic and inorganic contaminants provides valuable insight into real wastewater treatment. Knowledge gaps, uncertainties, and future challenges involved in the fabrication and regeneration of modified clay composites are also identified. | |
| 02/01/2019 00:00:00 | |
| Link to Article | |
| 2.10.2 | biochar |
| Application of oily sludge-derived char for lead and cadmium removal from aqueous solution | |
| Abstract The objective of this study was to investigate the physicochemical properties of oily sludge-derived char produced from pyrolysis at 500 °C (OS500) and its sorption behavior towards lead (Pb2+) and cadmium (Cd2+) in aqueous solution. The sorption kinetics and isotherm of Pb2+ and Cd2+ sorption on OS500 were determined. The results were fitted with four kinetic (pseudo first order, pseudo second order, Elovich equation, and intraparticle diffusion) and six isotherm (Langmuir, Freundlich, Sips, Redlich-Peterson, Temkin, and Dubinin-Radushkevich) models. The maximum sorption capacity ( Q L ) of Pb2+ obtained from the Langmuir model was 373.2 mg/g, while Q L of Cd2+ was 23.19 mg/g. The mechanisms of lead and cadmium sorption on OS500 and their quantitative contributions were further studied by Fourier transform infrared spectroscopy (FTIR), X-ray diffraction (XRD) and sequential extraction test. The results indicated the chemical characteristics (e.g., alkaline minerals and effective cation exchange capacity (CEC)) but not microstructure of OS500 controlled its Pb2+ and Cd2+ sorption. New mineral precipitates (i.e., hydrocerussite (Pb3(CO3)2(OH)2) and cerussite (PbCO3)) formed during Pb2+ sorption. The Pb2+-π interaction and complexation of Cd2+ with hydroxyl functional groups were evidenced by FTIR. Mineral precipitation with Pb2+ was the predominant mechanism for Pb2+ sorption on OS500 (accounted for 93.79%), whereas the complexation dominated Cd2+ sorption (accounted for 84.15%). The OS500 shows application potential in removing heavy metal contaminants from solution, especially Pb2+. | |
| 11/01/2019 00:00:00 | |
| Link to Article | |
| 2.10.3 | biochar |
| Enhanced nitrate removal by novel bimetallic Fe/Ni nanoparticles supported on biochar | |
| Abstract In this study, a novel bimetallic iron/nickel nanoparticles supported on biochar (BC@Fe/Ni) was established to degrade nitrate pollution in water. The nanocomposite was prepared from steel pickling waste liquor and sugarcane bagasse, which are made at low cost. The particle sizes of the nanocomposite ranged from about 10 nm to 20 nm and its specific surface area (59.83 m 2 /g) was about 71% bigger than that of nanoscale zero valent iron prepared from steel pickling waste liquor (S-NZVI), which proved that biochar had an excellent dispersal effect on bimetallic iron/nickel particles. Without controlling the pH, high nitrate removal rates over 93% could be realized in nitrate concentrations below 50 mg/L. The results of batch experiments demonstrated that the kinetics curves fitted the pseudo-first-order reaction well. And it was also found that higher dosages of the nanocomposite, lower initial nitrate concentrations, and acid medium facilitated nitrate degradation. In addition, the observed pseudo-first order rate coefficient in nitrate (20 mg/L) degradation rate by 4 g/L of the bimetallic iron/nickel supported on biochar was 30% faster than that by 2 g/L the bimetallic iron/nickel nanoparticles, due to the existence of biochar. And it was 75% faster than that by 2 g/L the nanoscale zero valent iron due to the existence of both biochar and the nanoscale zero valent nickel catalyst. Furthermore, iron and nickel ion pollution occurred in the denitrification system with bimetallic iron/nickel nanoparticles but not in that with the bimetallic iron/nickel nanoparticles supported on biochar, due to the biochar’s adsorption. After denitrification by the bimetallic iron/nickel nanoparticles supported on biochar, most of nitrate turned into ammonia (17.04 mg/L) and there only was a small amount of nitrite (0.024 mg/L) with high nitrate removal rate (99.5%). And most of ammonia can be absorbed by cation exchange resin with finial ammonia concentration of 0.58 mg/L. At last, the concentrations of nitrate (0.24 mg/L), nitrite (0.021 mg/L), and total nitrogen (0.84 mg/L) were lowest in the nanocomposite system. Overall, the bimetallic iron/nickel nanoparticles supported on biochar exhibited clear advantages over bimetallic iron/nickel nanoparticles and nanoscale zero valent iron with respect to degrading nitrate efficiently, preventing iron and nickel pollution and removing ammonia pollution in combination with cation exchange resin. | |
| 05/01/2017 00:00:00 | |
| Link to Article | |
| 2.10.4 | biochar |
| Enhanced removal of heavy metal ions from aqueous solution using manganese dioxide-loaded biochar: Behavior and mechanism. | |
| In this study, a redox precipitation method was used to load manganese dioxide (MnO2) nanoparticles on biochar (BC) (BC@MnO2) pyrolyzed from the invasive water hyacinth, and the adsorption of Cd(II),Cu(II), Zn(II), and Pb(II) was investigated. Several techniques were used to characterize the adsorbents. The results revealed that the BC surface was covered by many intertwined thin amorphous MnO2 nanosheets, which significantly increased its specific surface area and pore volume. The adsorption of heavy metal ions by BC was negligible, whereas the MnO2-containing adsorbents exhibited a high capacity for adsorbing heavy metal ions. However, the MnO2-normalized adsorption amount decreased with increasing MnO2 load and was largely unchanged at MnO2 loads of 26.6% to 30.2%. The capacity for adsorbing heavy metal ions of BC@MnO2 was pH-dependent, but the adsorption affinity was unaffected by coexisting ions. Column tests revealed that BC@MnO2 with a load of 26.6% had a high capacity for removing heavy metal ions from simulated and real electroplating wastewater. Therefore, BC@MnO2 with a load of 26.6% shows promise as a regenerable adsorbent for removing heavy metal ions from water/wastewater. This study could lay an essential foundation to develop a win-win strategy for heavy metal ions removal from wastewater using biochar derived from water hyacinth. | |
| 04/08/2020 00:00:00 | |
| Link to Article | |
| 2.10.5 | biochar |
| Novel Use of Dairy Processing Sludge Derived Pyrogenic Char (DPS-PC) to Remove Phosphorus in Discharge Effluents | |
| Purpose Pyrogenic char (PC) materials derived from the pyrolysis of dairy processing sludge (DPS) could be a cost effective option to develop carbonaceous adsorbent for phosphorus (P) removal from wastewater. The main objectives of the present work were to: (1) determine the efficacy of DPS derived PC (DPS-PC) to remove P from synthetic and dairy wastewater samples, (2) identify possible P removal mechanisms, and identify parameters that could be used to quickly identify the P removal capacity of a char and (3) propose a ranking system for the selection of DPS-PC which includes energy, char yield and P removal criterion. | |
| 07/01/2019 00:00:00 | |
| Link to Article | |
| 2.10.6 | biochar |
| Potential of Novel Biochars Produced from Invasive Aquatic Species Outside Food Chain in Removing Ammonium Nitrogen: Comparison with Conventional Biochars and Clinoptilolite | |
| Previous studies for removal of ammonium from wastewater were mainly conducted using biochars produced from agricultural residue. Feedstock type (agricultural residue, wood, animal waste, and aquatic waste), as well as pyrolysis temperature, can significantly influence biochar properties and hence its adsorption capacity. Such studies are useful in decision making for selecting biochar depending on feedstock availability and pyrolysis temperature. This study aims to explore the effects of different types of biochar (laboratory prepared novel water hyacinth and algae biochar, conventional cedar wood, rice straw, and pig manure biochar) on the adsorption kinetics for ammonium removal from wastewater. The adsorption kinetics of biochars were compared to that of commercially available clinoptilolite and interpreted with their respective physicochemical properties (SEM, FTIR, XRD). Batch tests were performed to evaluate the effects of biochars on adsorption of ammonium nitrogen at different concentrations (10 mg/L and 100 mg/L). The tests reveal that clinoptilolite has the highest adsorption capacity. Among biochars, pig manure (animal based) biochar has a higher adsorption capacity in comparison to conventional agricultural residues based biochars. The capacity of pig manure biochar under highly concentrated ammonium solution (100 mg/L) is merely 20% lower than that of clinoptilolite. Both water hyacinth and algae biochar produced at higher temperature (600 °C) show higher sorption rate and capacity (depending on the initial concentration of ammonium) for ammonium in comparison to that produced at a lower temperature (300 °C). This is likely due to an increase in porosity at higher temperatures of pyrolysis. | |
| 12/12/2019 00:00:00 | |
| Link to Article | |
2.11 Organic waste materials
It is reported that there are many agricultural and biological wastes materials can be used as adsorbents for the removal of heavy metals from wastewater. **New resources such as rice husk, eggshell, Moringa pods, bamboo leaf powder, cashew nut shells, palm oil fruit shells, and barley straw show great capacity of heavy metal removal.**
**Highlights:**
* And there are many materials which were studied including the mechanism, kinetic, and efficiency. The kinetic test of **Moringa pods** demonstrates that biosorption equilibrium reached within 30 min for nickel and 40 min for copper and chromium, respectively. **Bamboo leaf powder** modified by using anionic surfactant SDS and non-ionic surfactant Triton X-100 achieved the maximum adsorption of mercury around 30 mg/g. Rice husk can be fruitfully used for the removal of heavy metals with a concentration range of 20–60 mg/L. The removal of Pb and Cu can reach 100 % at pH 10 by **palm fruit shells**, while the maximum adsorption of Pb by **okra waste** was optimized at pH 5. Based on Langmuir isotherm, the maximum adsorption of Cu, Cd, Zn, and Ni was 406.6, 436.7, 455.7, and 456.3 mg/g by using **cashew nut shells**.[\[Paper\]](https://link.springer.com/article/10.1007%2Fs00253-016-7646-x)
* Therefore, this study investigated whether **inexpensive humic substances (HS) from sewage sludge compost could effectively remove copper (Cu) and cadmium (Cd) from highly contaminated sandy clay loam (S1) and clay (S2).** [\[Art. #ARTNUM\]](#article-96093-281661659)
* **Many types of lignocellulosic biomass show effective binding of toxic heavy metals from industrial and environmental effluents.** Biosorption is an emerging option for conventional methods to remove heavy metals, some of them with even better efficiencies compared to conventional methods. Raw material for biosorption is typically low-cost and easily available, including agricultural waste or forest residues such as sawdust, bark, or needles. **This review concentrates on the accumulation of heavy metals by lignocellulosic biosorbents.** Thus far, biosorption has not been economically feasible on a large scale and needs further development for profitability. Industrial-scale wood-based biosorbent applications are especially still lacking. Moreover, due to legislative demands, there is an increasing need for accurate and reliable analytical methods for metal analysis of environmental and industrial effluents. In the future, biosorption processes are likely to become common, and the requirement for environmental monitoring will increase due to ever restricting regulations. [\[Art. #ARTNUM\]](#article-96093-2920469717)
| 2.11.1 | Organic waste materials |
|---|---|
| Biosorption of heavy metals by lignocellulosic biomass and chemical analysis | |
| Many types of lignocellulosic biomass show effective binding of toxic heavy metals from industrial and environmental effluents. Biosorption is an emerging option for conventional methods to remove heavy metals, some of them with even better efficiencies compared to conventional methods. Raw material for biosorption is typically low-cost and easily available, including agricultural waste or forest residues such as sawdust, bark, or needles. This review concentrates on the accumulation of heavy metals by lignocellulosic biosorbents. Thus far, biosorption has not been economically feasible on a large scale and needs further development for profitability. Industrial-scale wood-based biosorbent applications are especially still lacking. Moreover, due to legislative demands, there is an increasing need for accurate and reliable analytical methods for metal analysis of environmental and industrial effluents. In the future, biosorption processes are likely to become common, and the requirement for environmental monitoring will increase due to ever restricting regulations. This emphasizes not only the need for the development of feasible process solutions, but also a requirement for accurate analytical methods. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
| 2.11.2 | Organic waste materials |
| Biosorption of heavy metals-An overview | |
| During the last two decades, extensive attention has been paid on the management of environmental pollution causal by hazardous materials such as heavy metals. Decontamination of heavy metals in the soil and water around industrial plants has been a challenge for a long time. A number of methods have been developed for the removal of heavy metals from liquid wastes such as precipitation, evaporation, electroplating, ion exchange, membrane processes, etc. However, these methods have several disadvantages such as unpredictable metal ion removal, high reagent requirement, generation of toxic sludge, etc. Biosorption is a process, which represents a biotechnological innovation as well as a cost effective excellent tool for removing heavy metals from aqueous solutions. This article provides a selective overview of past achievements and present scenario of biosorption studies carried out on some promising natural biosorbents (algae, fungi, bacteria, yeast) and some waste materials which could serve as an economical means of treating effluents charged with toxic metallic ions. | |
| 09/13/2008 00:00:00 | |
| Link to Article | |
| 2.11.3 | Organic waste materials |
| Humic substances from sewage sludge compost as washing agent effectively remove Cu and Cd from soil | |
| Although commercially available biosurfactants are environmentally friendly and effectively remove heavy metals from soil, they are costly. Therefore, this study investigated whether inexpensive humic substances (HS) from sewage sludge compost could effectively remove copper (Cu) and cadmium (Cd) from highly contaminated sandy clay loam (S1) and clay (S2). The optimum HS concentration and pH were determined, as well process kinetics. Under optimum conditions, a single washing removed 80.7% of Cu and 69.1% of Cd from S1, and 53.2% and 36.5%, respectively, from S2. Triple washing increased removal from S1 to almost 100% for both metals, and to 83.2% of Cu and 88.9% of Cd from S2. Triple washing lowered the potential ecological risk (Eri) of the soils, especially the risk from Cd. HS substances show potential for treating soils highly contaminated with heavy metals, and HS from other sources should be tested with these and other contaminants. | |
| 10/01/2015 00:00:00 | |
| Link to Article | |
2.12 Biosorption
Biosorption is sorption using (usually inactive) biomass. Numerous studies have been carried out with bacterial, fungal and algal biomass as biosorbents. Here the biomass does not actively take up the pollutants (as in bioleaching).
**Highlights:**
* Biosorption using algae biomass can be an alternative method to eliminate heavy metals. The objective of the project is to investigate the capability of Marine Algae (MA) and Freshwater Algae (FA) biomass in adsorbing heavy metals of Cu, Pb, Zn and Cd from water medium using synthetic water and industrial water. The result showed that FA and MA had a higher capability in adsorbing a total metal of about 40 ppm level from an industrial water, or 4 times than synthetic water concentration, at the same adsorbent dosage of 50 mg. In con-clusion, the presence of various functional groups, hydroxyl, carboxylic and amine groups, in all MA and FA samples had enabled the algae biomass to adsorb heavy metals of Cu, Pb, Cd and Zn from synthetic and industrial water. Due to their bio-sorptive properties and fast adsorption capability, algae could be a potential method for cleaning up surface water or post-treatment of wastewater and minimise the cost of eutrophication.[ \[Art. #ARTNUM\]](#article-96076-2540464837)
* Biosorption method by microalgae is one of the newest methods which have the properties such as cost, selective adsorption, high processing rate and no sludge production. In this process in order to clean up wastewater by adsorption, the two algae Chlorella and Spirulina are optimal. In comparing these two algaes, Chlorella algaehas better ability to attract as well as more balanced with the absorption effect. [\[Art. #ARTNUM\]](#article-96076-2268465717)
* A variety of biomaterials are known to bind these pollutants, including bacteria, fungi, algae, and industrial and agricultural wastes. In this review, the biosorption abilities of bacterial and fungal biomass towards metal ions are emphasized. [\[Art. #ARTNUM\]](#article-96076-2185808385)
| 2.12.1 | Biosorption |
|---|---|
| A comparative study of phosphorus removal using biopolymer from aerobic granular sludge: A factorial experimental evaluation | |
| Abstract This work presented an integrated approach to recover nutrients and biomaterials from wastewater, resulting in a phosphorus-enriched biomaterial with the potential for additional applications. The present investigation explored phosphorus removal from liquid samples using ALE recovered from aerobic granular sludge. The pH of the phosphorus solution, dosage of ALE beads, temperature and initial phosphorous concentration were factors tested through a factorial experimental design, with the results compared with commercial seaweed alginate. The ALE recovery from discarded aerobic sludge granules was 21.29 ± 1.57%. ALE beads demonstrated the potential to remove phosphorus (49.54 ± 2.23%) from liquid samples better than commercial seaweed alginate (36.78 ± 2.10%). The results from the factorial experiment indicated pH and dosage of ALE beads as the main parameters for phosphorus removal. Regeneration of ALE beads and the phosphorus recovery experiments showed the potential of using this biomaterial as a biodegradable phosphorus slow-release source. | |
| 11/01/2019 00:00:00 | |
| Link to Article | |
| 2.12.2 | Biosorption |
| Biosorption of Heavy Metal by Algae Biomass in Surface Water | |
| Discharging wastewater containing heavy metals of Cu, Pb, Zn and Cd into water bodies can cause toxicity in plants and aquatic animals and some of them will be unable to survive except algae. Wastewater treatment method to remove heavy metal contaminants includes chemical precipitation, ion exchange, membrane, filtration, adsorption using activated carbon. However, these methods are either expensive or have other disadvantages such as high energy consumption and inefficiencies when existing heavy metals are at trace concentration. Biosorption using algae biomass can be an alternative method to eliminate heavy metals. The objective of the project is to investigate the capability of Marine Algae (MA) and Freshwater Algae (FA) bi-omass in adsorbing heavy metals of Cu, Pb, Zn and Cd from water medium using synthetic water and industrial water. MA and FA were obtained from the eastern coast of Pulau Ubin and local fish farm respectively. After being fully washed with deionised water, dried in a furnace for 105°C, they are grinded to pass 1 mm2 of siever. MA and FA were characterised using FTIR to determine their functional groups. An industrial water was collected from industrial discharge from metal fac-tories in northern side of Singapore. Effect of adsorption time, adsorbent concentra-tion, and pH were studied. The result showed that FA and MA had a higher capability in adsorbing a total metal of about 40 ppm level from an industrial water, or 4 times than synthetic water concentration, at the same adsorbent dosage of 50 mg. In con-clusion, the presence of various functional groups, hydroxyl, carboxylic and amine groups, in all MA and FA samples had enabled the algae biomass to adsorb heavy metals of Cu, Pb, Cd and Zn from synthetic and industrial water. Due to their bio-sorptive properties and fast adsorption capability, algae could be a potential method for cleaning up surface water or post-treatment of wastewater and minimise the cost of eutrophication. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 2.12.3 | Biosorption |
| Biosorption of heavy metals by lignocellulosic biomass and chemical analysis | |
| Many types of lignocellulosic biomass show effective binding of toxic heavy metals from industrial and environmental effluents. Biosorption is an emerging option for conventional methods to remove heavy metals, some of them with even better efficiencies compared to conventional methods. Raw material for biosorption is typically low-cost and easily available, including agricultural waste or forest residues such as sawdust, bark, or needles. This review concentrates on the accumulation of heavy metals by lignocellulosic biosorbents. Thus far, biosorption has not been economically feasible on a large scale and needs further development for profitability. Industrial-scale wood-based biosorbent applications are especially still lacking. Moreover, due to legislative demands, there is an increasing need for accurate and reliable analytical methods for metal analysis of environmental and industrial effluents. In the future, biosorption processes are likely to become common, and the requirement for environmental monitoring will increase due to ever restricting regulations. This emphasizes not only the need for the development of feasible process solutions, but also a requirement for accurate analytical methods. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
| 2.12.4 | Biosorption |
| Biosorption of heavy metals-An overview | |
| During the last two decades, extensive attention has been paid on the management of environmental pollution causal by hazardous materials such as heavy metals. Decontamination of heavy metals in the soil and water around industrial plants has been a challenge for a long time. A number of methods have been developed for the removal of heavy metals from liquid wastes such as precipitation, evaporation, electroplating, ion exchange, membrane processes, etc. However, these methods have several disadvantages such as unpredictable metal ion removal, high reagent requirement, generation of toxic sludge, etc. Biosorption is a process, which represents a biotechnological innovation as well as a cost effective excellent tool for removing heavy metals from aqueous solutions. This article provides a selective overview of past achievements and present scenario of biosorption studies carried out on some promising natural biosorbents (algae, fungi, bacteria, yeast) and some waste materials which could serve as an economical means of treating effluents charged with toxic metallic ions. | |
| 09/13/2008 00:00:00 | |
| Link to Article | |
| 2.12.5 | Biosorption |
| Biosorption, an efficient method for removing heavy metals from industrial effluents: A Review | |
| Abstract Common methods for removing heavy metals have numerous drawbacks, including low efficiency and high costs. In the biosorption of heavy metals, ions biosorbed on surfaces and active sites of biosorbents. In this paper, the relationship between the factors (pH, temperature, biosorbent dosage, retention time and Functional groups) and removal efficiency has been investigated. The purpose of this work is to introduce optimal conditions for biosorption reaction. Also, by introducing various types of biosorbents, expressed the advantages and method of preparation for each one. In various papers, not all biosorption isotherm models have been mentioned, there are described various types of biosorption isotherm, kinetics and thermodynamics models and important process data is set up for quick access to the tables. | |
| 02/01/2020 00:00:00 | |
| Link to Article | |
| 2.12.6 | Biosorption |
| Characteristics and function of macroalgae biosorption technology to metal ion | |
| Biosorption is a new technique which utilizes inexpensive living/dead organisms(fungi or algae) to adsorb heavy metals and is particularly useful for the removal of contaminants from industrial effluents. Compared with conventional methods such as ion exchange and precipitation with lime , the biosorption technique offers the advantages of low operating cost, minimization of the less disposed volume of chemical and biological sludge and high efficiency in detoxifying very dilute effluents. These advantages have served as the incentives for developing full biosorption technique to clean up heavy metal pollution. Biosorption technology is just developing rapidly, and is attractting more and more attention from scientists over the world, and we hope this technology will be extensively applied in our country. | |
| 01/01/2003 00:00:00 | |
| Link to Article | |
| 2.12.7 | Biosorption |
| Comparative Study of Rates of Biosorption for Selected Single and Mixed Metal Ions using Natural Products | |
| Heavy metals are usually found in low concentrations in natural aquatic ecosystem. In recent times, however, the occurrence of metal contaminants especially heavy metals in excess of natural loads has become a problem of increasing concern. The contributing factors are rapid growth of population, increased urbanization and expansion of industrial activities, exploration and exploitation of natural resources, extension of irrigation and other modern agricultural practices as well as lack of environmental regulations. This therefore, calls for efficient, cheap, available and non polluting method of controlling presence of heavy metals in water bodies. Use of natural biosorbents such as algae has demonstrated great potential to remove heavy metals from wastewater. An investigation of the effect of contact time, reaction kinetics, influence of ionic sizes and influence of presence of other metal ions in biosorption of heavy metals Cu, Zn and Pb using Ascophyllum nodosum has been done. Model wastewater solution containing a known concentration of the given heavy metal ions was prepared for both single and mixed at a fixed pH of 5. A 0.25g mass of dry algae was introduced for every 100 mL solution. Change in level of concentration was monitored at intervals of 10 minutes using AAS until the rate of biosorption was almost constant. The sorption process occurred in two stages; first being rapid adsorption and then gradual adsorption that was almost constant. Pb was most biosorbed while Zn was least for both systems, adopting the order Pb > Cu > Zn. The data obtained fitted both Langmuir isotherm and experimental parameters were determined. The order of reaction was found to follow pseudo second order after comparison of R2 values that were deduced from first and second order linearized plots.Key words: Biosorption, heavy metals, algae, wastewater, pollution | |
| 01/01/2013 00:00:00 | |
| Link to Article | |
| 2.12.8 | Biosorption |
| Different methods to adsorb heavy metals in wastewater by blue-green algae | |
| Background: Among the today`s main problems related to wastewater is pollution caused by heavy metals. These heavy metals are toxic and have detrimental effects on the body. So the existence of such metals in the food chain is a serious problem for human health. Materials and Methods: Scopus, Pubmed, Google scholar and ScienceDirect databases were searched. Results: Studies indicate a requirement to use a new method for removing heavy metals from wastewater. Biosorption method by microalgae is one of the newest methods which have the properties such as cost, selective adsorption, high processing rate and no sludge production. In this process in order to clean up wastewater by adsorption, the two algae Chlorella and Spirulina are optimal. In comparing these two algaes, Chlorella algaehas better ability to attract as well as more balanced with the absorption effect. Remove ions such as lead, nickel and zinc occurs by interactions between the metal ions and carboxyl groups present on the cell wall that stabilize metal binding. Notable point in this process is that the removal ability decreases by increasing the metal concentration. In addition, Chlorella can be used to adsorb Chromium that Betacaroten first extracted and then the remaining biomass is used for Chromium adsorption. Conclusions: According to the case studies, the method is convenient and cost effective for the removal of metal contaminants from wastewater and will help to reduce environmental pollution. | |
| 03/15/2013 00:00:00 | |
| Link to Article | |
| 2.12.9 | Biosorption |
| Keratin Protein Nano-fiber for Removal of Heavy Metals and Contaminants | |
| ABSTRACT Keratin protein fiber (AKF TM ) is a renewable source of biosorbent that can be used for filtration of heavy metal and nanosize contaminants. The major composition of keratin fiber is the structured protein micofibril, consisting of numerous nanosized pores. The combination of nanostructure and metal binding capacity protein sites make it an ideal material for removal of heavy metals from solutions. The mechanism of heavy metal uptake onto keratin protein involves a combination of several steps such as adsorption, precipitation, and ion exchange. Keratin protein has good tensile strength and is stable over a wide pH range. INTRODUCTION & BACKGROUND Conventional methods for removing heavy metals from contaminated solutions include chemical precipitation, carbon adsorption, membrane separation, microfiltration and the use of ion exchange resins. Many of the existing technologies for the removal of heavy metals from wastewaters are unable to achieve the low final concentrations required by new regulations. Furthermore, many existing treatment processes merely convert aqueous metal ions into solid sludges, which require costly landfill disposal. Biosorption, a relatively simple metal adsorption process, can meet the progressively stricter environmental discharge criteria. The term "biosorption" is used to describe the accumulation of metal ions by adsorption and/or ion exchange from solutions by materials of biological origin, particularly microorganisms, plant biomass and animal cells and extracts [1]. Thus the potential use of materials of biological origin in the treatment of heavy metal-contaminated wastewaters is of special importance. Organisms such as algae, bacteria, fungi, and yeasts have proved to be potential metal sorbents [1] | |
| 01/01/2001 00:00:00 | |
| Link to Article | |
| 2.12.10 | Biosorption |
| Microbial Biosorption as a Green Technology for Bioremediation of Heavy Metals. | |
| The exponential growth of Industrialization with the increase in human population has led to a heavy metal pollution problem, which has become ubiquitous from air to soil. Heavy metal pollution has become a more serious environmental problem in the last several decades as a result of its toxicity and insusceptibility to the environment. There are many bioremediation technologies including biosorption process to decontaminate the heavy metal polluted sites. Biosorption is a technique that can be used for the removal of pollutants from waters, especially those that are not easily biodegradable such as metals and dyes. A variety of biomaterials are known to bind these pollutants, including bacteria, fungi, algae, and industrial and agricultural wastes. In this review, the biosorption abilities of bacterial and fungal biomass towards metal ions are emphasized. This review attempts to present a brief summary of the role of biosorption in heavy metal removal from wastewater. Undoubtedly, the biosorption process is a potential technique for heavy metal decontamination. | |
| 01/01/2015 00:00:00 | |
| Link to Article | |
| 2.12.11 | Biosorption |
| Potential of biosorption and bioaccumulation processes for heavy metals removal in bioreactors | |
| Environmental contamination with heavy metals, especially of soils and water, became a significant problem because most of them are toxic to the living organisms, non-degradable and persistent in the contaminated media. Physico-chemical methods, such as chemical precipitation, electrochemical treatment, filtration, ion exchange, evaporation, reverse osmosis and membrane technologies are currently the most used methods to remove heavy metal ions from wastewaters. Bioremediation technologies, which are known to be environmentally sound natural processes, have become attractive alternatives to the conventional methods. Among these, biosorption and bioaccumulation address various interactions and concentration of toxic metals in either living (bioaccumulation) or non-living (biosorption) biomass. The aim of this paper is to emphasize the proficiency of biosorption and bioaccumulation processes applied in different types of bioreactors (stirred tank, fixed bed, fluidized-bed and air-lift) using various microorganisms for the removal of heavy metals from contaminated effluents. | |
| 11/01/2015 00:00:00 | |
| Link to Article | |
| 2.12.12 | Biosorption |
| Removal of chromium (VI) by Escherichia coli cells expressing cytoplasmic or surface-displayed ChrB: a comparative study. | |
| Various genetically engineered microorganisms have been developed for the removal of heavy metal contaminants. Metal biosorption by whole-cell biosorbents can be enhanced by overproduction of metal-binding proteins/peptides in the cytoplasm or on the cell surface. However, few studies have compared the biosorption capacity of whole cells expressing intracellular or surface-displayed metal-adsorbing proteins. In this study, several constructs were prepared for expressing intracellular and surface-displayed Ochrobactrum tritici 5bvl1 ChrB in Escherichia coli BL21(DE3) cells. E. coli cells expressing surface-displayed ChrB removed more Cr(VI) from aqueous solutions than cells with cytoplasmic ChrB under the same conditions. However, intracellular ChrB was less susceptible to variation in extracellular conditions (pH and ionic strength), and more effectively removed Cr(VI) from industrial wastewater than the surface-displayed ChrB at low pH (<3). An adsorption-desorption experiment demonstrated that compared with intracellular accumulation, cell-surface adsorption is reversible, which allows easy desorption of the adsorbed metal ions and regeneration of the bioadsorbent. In addition, an intrinsic ChrB protein fluorescence assay suggested that pH and salinity may influence the Cr(VI) adsorption capacity of ChrB-expressing E. coli cells by modulating the ChrB protein conformation. Although the characteristics of ChrB may not be universal for all metal-binding proteins, our study provides new insights into different engineering strategies for whole-cell biosorbents for removing heavy metals from industrial effluents. | |
| 03/20/2020 00:00:00 | |
| Link to Article | |
| 2.12.13 | Biosorption |
| Synthesis of biosorbents from natural/agricultural biomass wastes and sustainable green technology for treatment of nanoparticle metals in municipal and industrial wastewater | |
| Abstract Municipal and industrial wastewaters, manufacturing of electrical and electronic equipment, etc., are spreading toxic heavy metals such as lead, arsenic, zinc, nickel, cadmium, uranium, and mercury in the aquatic and soil environment. There are some traditional treatment technologies to remove heavy metals from drinking water and wastewater. However, conventional treatment technologies are expensive and not always efficient for the treatment of wastewaters with high metal concentration. Furthermore, these methods need more chemicals and energy and produce toxic sludge. By contrast, bioremediation by biosorption process using biosorbents is a low-cost, highly efficient, easy operating, eco-friendly, and sustainable green technology for the removal of heavy metals from wastewater. The renewable biocomposite biosorbent materials can be prepared from plant biomass; agricultural wastes such as fruit peels, straw, and coconut coir; bacteria; yeasts; fungi; and algae. The main mechanisms of biosorption process involve ion exchange, surface complexation, adsorption, absorption, and precipitation methods. Biosorption has several benefits, such as selective removal of metals, biosorbent regeneration and metal recovery, rapid kinetics of adsorption and desorption, and no sludge generation. The biosorbent materials can be modified by different physical and chemical treatments and other treatments to prepare novel adsorbents and remove nanoparticle heavy metal contaminants from wastewater. The biosorbents without treatment have shown low adsorption capacity. The chemical pretreatments significantly improved the adsorption capacities of biosorbents by increasing the number of binding sites, ion-exchange ability, and new functional groups. The main composition of plant biomass and agricultural waste consists of cellulose, hemicellulose, and lignin containing different functional groups, such as hydroxyl groups, acetamido, carboxyl, phenolic, structural polysaccharides, amido, amino, sulfhydryl and carboxyl groups, alcohols, and ester. Some important physical and chemical factors influencing the biosorption of heavy metals from wastewater are pH, temperature, initial heavy metal concentration, biosorbent dose, biosorbent size, ionic strength, and coions. Nanoparticle heavy metals can be recovered from the biosorbents by physical treatment such as heating, stirring, and agitation or chemical treatments. The chemical treatments use the chemicals as eluents that include acid, alkali, and organic solvent. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
3. Electro-treatment
BackTreatments using electrical currents
3.1 Electrochemical
Electrochemical techniques, such as electrolysis use electrical currents to facilitate chemical reactions that can lead to separation.
**Highlights:**
* Electrochemical techniques have been extensively applied to treat heavy metal pollution in our daily life. Traditional electrochemistry is always driven by continuous DC (CDC), but the energy harvested in environment from water using nanogenerator is always a pulsed DC (PDC). Here, we systematically investigated the electrochemical performance of hexavalent chromium (Cr(VI)) removal from wasted as powered by pulsed output of triboelectric nanogenerator (TENG) using the energy harvested from environment. **By optimizing the frequency and on-off ratio of PDC, the removal efficiency of Cr(VI) can be maximally enhanced by 53.5% compared to that driven by a CDC under equal amount of electric charges, which is further confirmed by electrochemical experiments driven by layered TENG.** \[...\] This study demonstrate the feasibility and effectiveness of self-powered electrochemical for cleaning environment pollution using the harvested energy.[ \[Art. #ARTNUM\]](#article-96116-2963263812)
* Recently electrochemical process for removing phosphorous (P) from effluents has received more attention to control water resource pollution. The energy demand was 7.69 KWh per equivalent of removed P and 0.45 kWh/m3. The data showed that the proposed method is economical and certainly more efficient in comparison with conventional P removal methods. Therefore, the electrochemical process alone by steel electrodes may be a capable process for P removal from filtered activated sludge effluent. [\[Art. #ARTNUM\]](#article-96116-3015328989)
* Electrolytic recovery or electro-winning is one of the many technologies used to remove metals from process water streams. This process uses electricity to pass a current through an aqueous metal-bearing solution containing a cathode plate and an insoluble anode. Positively charged metallic ions cling to the negatively charged cathodes leaving behind a metal deposit that is strippable and recoverable. A noticeable disadvantage was that corrosion could become a significant limiting factor, where electrodes would frequently have to be replaced[\[Paper\]](https://www.sciencedirect.com/science/article/pii/S1878535210001334#:\~:text=2.3.&text=The%20conventional%20processes%20for%20removing,metal%20removal%20from%20inorganic%20effluent.)
| 3.1.1 | Electrochemical |
|---|---|
| Ammonia removal via microbial fuel cell (MFC) dynamic reactor | |
| Landfill leachate is generally known as high-strength wastewater that is difficult to handle and contains dissolved extracts and suspended matter. Microbial fuel cells (MFCs) were designed to treat landfill leachate while continuously producing power (voltage output). Three different anodes were tested in MFC reactors: carbon black, activated carbon, and zinc electrodes. Movements in the MFC reactor during treatment were also a key factor for testing. Results showed a difference in ammonia levels in the three anodes used. The study compared the efficiency of static and dynamic modes of MFC in removing ammonia. Continual leachate movement in the reactor could increase the rate of removal of the ammonia components. The setup provided a viable condition for maximum removal because the reactor movement caused the sludge to disintegrate, which allowed ammonia to separate easily from the parent leachate. Ammonia removal also resulted from the transfer of ammonium through the membrane or from ammonia loss. Constant exchange of ionic content benefited the MFC performance by increasing power production and decreasing internal electrode material resistance. This paper presents the results of the analyses of leachate treatment from the solid waste landfill located in Padang Siding Landfill, Perlis. The performance of ammonia removal was enhanced using different types of electrodes. In both modes, activated carbon performed better than black carbon and zinc. The respective percentages of ammonia removal for activated carbon of dynamic over static were 96.6%, 66.6%, and 92.8% for activated carbon, zinc, and black carbon. The results provide further information on the possibility of using MFCs in landfill leachate treatment systems. | |
| 06/01/2017 00:00:00 | |
| Link to Article | |
| 3.1.2 | Electrochemical |
| Application of Electrocoagulation and Electrolysis on the Precipitation of Heavy Metals and Particulate Solids in Washwater from the Soil Washing | |
| Soil washing, ex situ mechanical technique, is one of the few permanent treatment alternatives to remove metal contaminants from soils by employing physical separation based on mineral processing technologies to remove discrete particles or metal-bearing particles and/or chemical extraction based on leaching or dissolving process to extract the metals from the soils into an aqueous solution. However, washwater remained from soil washing process contains discrete particulate particles along with heavy metals as solution phase to be treated separately, as well as this process can produce large amount of sludge that requires further treatment, slow metal precipitation, poor settling, the aggregation of metal precipitates. Electrical treatments including electrocoagulation and electrolysis can be effective in removing these substances from washwater. This paper reviews the theoretical models in applying electrocoagulation and electrolysis to remove heavy metals and discrete particulate particles in washwater by examining and comparing the status of washwater treatment technologies which have been undertaken, mostly in the US and EU for the period 1990-2012. | |
| 01/01/2014 00:00:00 | |
| Link to Article | |
| 3.1.3 | Electrochemical |
| Comparison of bioleaching and electrokinetic remediation processes for removal of heavy metals from wastewater treatment sludge | |
| Abstract Heavy metals prevent the growing amount of sewage sludge from being disposed as fertilizeron land. The electrokinetic remediation and bioleaching technology are the promising methods to remove heavy metals. In recent years, some innovation has been made to achieve better efficiency, including the innovation of processes and agents. This paper reviews the development of the electrokinetic remediation and bioleaching technology and analyses their advantages and limitation, pointing out the need of the future research for the heavy metals-contaminated sewage sludge. | |
| 02/01/2017 00:00:00 | |
| Link to Article | |
| 3.1.4 | Electrochemical |
| Direct/Alternating Current Electrochemical Method for Removing and Recovering Heavy Metal from Water Using Graphene Oxide Electrode | |
| Treatment of heavy-metal pollution in both point-of-use water and industrial wastewater is critical in protecting human health and the environment. Current methods for heavy-metal treatment in both sources have limitations. For point-of-use water, current methods usually suffer from limited capacity and difficulties in spontaneously removing multiple heavy metals. For industrial wastewater, current methods greatly reduce the value of heavy metal by precipitating them as sludge which requires further treatment. Here we developed an electrochemical method that can treat both low-concentration and high-concentration heavy-metal pollution using either direct current (DC) or alternating current (AC) electrodeposition with graphene-oxide-modified carbon felt electrode (CF-GO). The graphene oxide provides a high density of surface functional groups to assist the electrodeposition. The electrodeposition method showed 2 orders of magnitude higher capacity (>29 g heavy metal for 1 g of graphene oxide) compared with... | |
| 05/22/2019 00:00:00 | |
| Link to Article | |
| 3.1.5 | Electrochemical |
| Effective removing of hexavalent chromium from wasted water by triboelectric nanogenerator driven self-powered electrochemical system – Why pulsed DC is better than continuous DC? | |
| Abstract Electrochemical techniques have been extensively applied to treat heavy metal pollution in our daily life. Traditional electrochemistry is always driven by continuous DC (CDC), but the energy harvested in environment from water using nanogenerator is always a pulsed DC (PDC). The question is if the CDC has a better performance than PDC? Here, we systematically investigated the electrochemical performance of hexavalent chromium (Cr(VI)) removal from wasted as powered by pulsed output of triboelectric nanogenerator (TENG) using the energy harvested from environment. By optimizing the frequency and on-off ratio of PDC, the removal efficiency of Cr(VI) can be maximally enhanced by 53.5% compared to that driven by a CDC under equal amount of electric charges, which is further confirmed by electrochemical experiments driven by layered TENG. The reason is the more production of Fe 2+ , the better utilization of Fe 2+ , and the higher ion diffusion rate during the process driven by PDC, where the electrode passivation caused by concentration polarization of the anode region and over potential is reduced. Besides, a self-powered system is designed for removing contaminant from wastewater by harvesting energy from the flowing water through rotary-TENG, where heavy metal pollutant such as Cr(VI) can be sufficiently and continuously removed. This study demonstrate the feasibility and effectiveness of self-powered electrochemical for cleaning environment pollution using the harvested energy. | |
| 10/01/2019 00:00:00 | |
| Link to Article | |
| 3.1.6 | Electrochemical |
| Heavy metal removal from contaminated sludge for land application : A review | |
| In recent years, various methods for heavy metal removal from sewage sludge have been extensively studied in order to minimize the prospective health risks of sludge during land application. In this paper, a comparative review and critical analysis of the application of chemical extraction, bioleaching, electroreclamation, and supercritical fluid extraction (SFE), in removing heavy metals from contaminated sludges is presented. Moreover, speciation studies, which can indicate ease of leachability of the different forms of heavy metals in sludge, are also presented. Experimental studies revealed a broad range in metal extraction efficiencies of the different extraction technologies. Acid treatment seemed to effectively remove Cd, attaining as much as 100% removal for some studies, as compared to bioleaching. SFE also gave higher removal efficiency than bioleaching. Cr, Pb and Ni seemed to be also effectively removed by the acid treatment. For the removal of Cu, Mn and Zn, the bioleaching process seemed to be appropriate with maximum removal efficiencies of 91%, 93% and 96% for the three metals, respectively, and as high as 64% minimum removal efficiency for Zn. The SFE process also gave good results for Cu, Mn and Zn removal. Electroreclamation exhibited better removal efficiency for Mn, but is still inferior to acid treatment and bioleaching processes. For chemical extraction, because of the adverse impacts that can result from the use of inorganic acids and complexing agents, interest can be directed more toward utilizing organic acids as extracting agents because of their biodegradability and capability to remove metals at mildly acidic condition, hence requiring less acid. The bioleaching process, although it seems to give a higher yield of metal extraction with lower chemical cost than chemical extraction, may be limited by the inability of the system to cope with the natural environmental conditions, requires strict monitoring of aeration rate and temperature and has applicability to only low sludge solids concentration. A full-scale study would be useful to better assess the efficiency of the process. The electroreclamation technology is limited by its relatively higher energy consumption and limited applicability to sludge. The SFE method, on the other hand, is limited by the complexity of the process and the cost of ligands suitable for effective metal extraction. Both of these technologies are still in their early stage of application and hence there is a need for further basic and applied studies. Finally, the common advantage for almost all treatment technologies studied is that the extraction efficiencies for some metals are high enough to remove metals from sludge to levels suitable for land application. | |
| 01/01/2006 00:00:00 | |
| Link to Article | |
| 3.1.7 | Electrochemical |
| High-efficiency removal of phosphorous from filtered activated sludge effluent using electrochemical process | |
| Abstract Recently electrochemical process for removing phosphorous (P) from effluents has received more attention to control water resource pollution. However, there are many uncertainties about energy demand in this process. So, in this research energy demand was principally investigated. P concentration was measured on 210 samples before and after the electrochemical process. Direct current electricity was applied in the range of 0.1–1.5 A (A). Cathode and anode electrodes were eight pieces of steel plate submerged in the liquid. After measurement of P concentration, the data were analyzed by Greenhouse-Geisser, one-way ANOVA and Tukey's tests. The results showed that the optimum reaction time and electricity currents were 10 min and 0.6 A, respectively. Also, 98% efficiency for P removal was achieved. The current density was 1.89 mA/cm2. The energy demand was 7.69 KWh per equivalent of removed P and 0.45 kWh/m3. The data showed that the proposed method is economical and certainly more efficient in comparison with conventional P removal methods. Therefore, the electrochemical process alone by steel electrodes may be a capable process for P removal from filtered activated sludge effluent. | |
| 04/06/2020 00:00:00 | |
| Link to Article | |
| 3.1.8 | Electrochemical |
| Potential Electrokinetic Remediation Technologies of Laboratory Scale into Field Application- Methodology Overview | |
| Heavy metal in soil possesses high contribution towards soil contamination which causes to unbalance ecosystem. There are many ways and procedures to make the electrokinetic remediation (EKR) method to be efficient, effective, and potential as a low cost soil treatment. Electrode compartment for electrolyte is expected to treat the contaminated soil through electromigration and enhance metal ions movement. The electrokinetic is applicable for many approaches such as electrokinetic remediation (EKR), electrokinetic stabilization (EKS), electrokinetic bioremediation and many more. This paper presents a critical review on comparison of laboratory scale between EKR, EKS and EK bioremediation treatment by removing the heavy metal contaminants. It is expected to propose one framework of contaminated soil mapping. Electrical Resistivity Method (ERM) is one of famous indirect geophysical tools for surface mapping and subsurface profiling. Hence, ERM is used to mapping the migration of heavy metal ions by electrokinetic. | |
| 04/01/2018 00:00:00 | |
| Link to Article | |
| 3.1.9 | Electrochemical |
| Purification of wastewater from the ions of copper, zinc, and lead using an electrolysis method | |
| Heavy metals penetrate water reservoirs as a result of natural and anthropogenic processes, thereby accumulating in soil, bottom sediment, sludge, and can further migrate into groundwater and surface water. The main sources of heavy metals penetration into natural waters are the insufficiently treated waste waters from many branches of industry. That renders relevance to the problem of removing heavy metals from wastewater in order to prevent excessive pollution of water reservoirs. Among existing methods of water purification from heavy metals’ ions at significant volumes of industrial wastewater, the electrochemical methods are rather promising. The advantage of this method is a possibility to recycle the used regeneration solutions with obtaining metals that are suitable for reuse. This paper reports results of research into the processes of electrochemical removal of heavy metals’ cations from diluted aqueous solutions in oneand twochamber electrolyzers. When conducting the study in a twochamber electrolyzer, the anode and cathode regions were separated by the anionexchanging membrane MA40. A dependence of the influence of hardness, solutions’ pH, anodic current density, and the duration of electrolysis on efficiency of the removal of heavy metals’ ions was investigated. It is shown that the ions of zinc, copper and lead are effectively removed from aqueous solutions using the electrolysis at a starting concentration of 10 mg/dm3. It was established that at the low concentrations of ions, the output for current, when reducing metals, reached (4–20)·104 % and changed little with concentration. It was determined that the efficiency of water purification from heavy metals’ ions using electrolysis increases with an increase in pH of the medium and with a decrease in the hardness of water. In the twochamber electrolyzers, these factors exert almost no effect on purification efficiency. The paper shows the prospect of using electrolysis for the selective removal of heavy metals from tap, softened and natural water. A given purification method makes it possible to not only postclean wastewater to the maximally permissible concentrations, but also enables the purification of water from natural water bodies to the quality of drinking water | |
| 12/05/2018 00:00:00 | |
| Link to Article | |
3.2 Electrokinetic
In electrokinetic methods, compounds are separated based on their charge.
Electrophoresis and electroosmosis are two examples of electrokinetic methods, and its is also the pinciple behind electrodialysis (see [\[Electrodialysis\]](#technology-96117))
**Highlights:**
* **In this study, an ex situ method for removing heavy metals from sludge using electroosmosis** was designed, and experiments were conducted to study the effects of electroosmosis voltages (30 V, 40 V and 50 V), citric acid concentrations (0.03 mol/kg, 0.06 mol/kg, 0.09 mol/kg and 0.12 mol/kg) and the power supply (continuous and interrupted) on the removal rate of heavy metals (Cu, Cr, Cd, Zn and Pb). **The study found that the combination of the citric acid pretreatment and electroosmosis can effectively improve the removal rate of heavy metals.** [\[Art. #ARTNUM\]](#article-96089-3011564947)
* Sewage sludge ash is rich in phosphorus, but the direct use as fertilizer is limited because of inorganic contaminants such as heavy metals and strong bonding of phosphorous in the ash. **Electrodialysis (ED) can be used to recover phosphorus and simultaneously remove heavy metals.** Simplifying this experimental setup by removing the anion exchange membrane brings the anode in direct contact with the stirred ash suspension. Through this adjustment, half-reactions at the anode contribute to the acidity of the stirred suspension resulting in increased dissolution of both phosphorus and heavy metals (Cd, Cu, Cr, Pb, Zn, Ni) and better separation of most heavy metals from the stirred ash suspension. [\[Art. #ARTNUM\]](#article-96089-1980378680)
* The electrophoretic deposition (EPD) is found to be one of the potential techniques that can be used to minimize these issues.EPD is the process of colloidal particles and regularly carried out in two electrode cells that dispersed in suspension medium with the existence of electric field. To obtain the optimum condition of EPD; the pH, current, particle size of heavy metals, type of electrode, and voltage are determined key factors. [\[Art. #ARTNUM\]](#article-96089-2969982782)
* Dielectrophoresis (DEP) was combined with adsorption (ADS) to simultaneously and effectively remove Cd2+ and Pb2+ species from aqueous solution. To implement the process, bentonite particles of submicro-meter size were used to first adsorb the heavy metal ions. These particles were subsequently trapped and removed by DEP. The high removal efficiency, 97.3% and 99.9% for Cd2+ and Pb2+, respectively, were achieved when the ions are coexisting in the system. The microstructure of bentonite particles before and after ADS/DEP was examined by scanning electron microscopy. Our results suggest that the dielectrophoresis-assisted adsorption method has a high capability to remove the heavy metals from wastewater. [\[Art. #ARTNUM\]](#article-96089-2908932138)
| 3.2.1 | Electrokinetic |
|---|---|
| Application of electrophoretic deposition in capturing heavy metals from industrial wastewater to enhance health and environment aspects / Hartini Mahmood | |
| The industrial wastewater pollution is recognized to have a major negative impact on health and environment aspects. It’s mainly contributed by the generation of heavy metals which release to the water body after or during the manufacturing process. In terms of human health, the pollution from heavy metals will lead to serious diseases, while for the environment, the water crises and disturbance of aquatic life are the sequence from the heavy metals pollution. There are various types of water treatments availableto remove heavy metals such as chemical precipitation, ion exchange and membrane filtration. However, these treatments have limitations and weaknesses such as sludge generation, low selectivity, costly and some of them needadditional treatment to improve the removal efficiency.The electrophoretic deposition (EPD) is found to be one of the potential techniques that can be used to minimize these issues.EPD is the process of colloidal particles and regularly carried out in two electrode cells that dispersed in suspension medium with the existence of electric field. To obtain the optimum condition of EPD; the pH, current, particle size of heavy metals, type of electrode, and voltage are determined key factors.This study is to review the EPD process through several points of view, including the process principle, mechanism, effect of parameters and the exploration on EPD studies. A systematic review was used to answer a defined research question by collecting and summarizing all empirical evidence that fits pre-specified eligibility criteria.Additionally, several outlooks based on studies in the literature regarding to health and environmental effects from heavy metals are also presented in this paper. | |
| 07/01/2018 00:00:00 | |
| Link to Article | |
| 3.2.2 | Electrokinetic |
| Comparison of bioleaching and electrokinetic remediation processes for removal of heavy metals from wastewater treatment sludge | |
| Abstract Heavy metals prevent the growing amount of sewage sludge from being disposed as fertilizeron land. The electrokinetic remediation and bioleaching technology are the promising methods to remove heavy metals. In recent years, some innovation has been made to achieve better efficiency, including the innovation of processes and agents. This paper reviews the development of the electrokinetic remediation and bioleaching technology and analyses their advantages and limitation, pointing out the need of the future research for the heavy metals-contaminated sewage sludge. | |
| 02/01/2017 00:00:00 | |
| Link to Article | |
| 3.2.3 | Electrokinetic |
| Comparison of two different electrodialytic cells for separation of phosphorus and heavy metals from sewage sludge ash | |
| Abstract With decreasing availability of phosphorus from primary resources its recovery from waste streams becomes increasingly more important. Sewage sludge ash is rich in phosphorus, but the direct use as fertilizer is limited because of inorganic contaminants such as heavy metals and strong bonding of phosphorous in the ash. Electrodialysis (ED) can be used to recover phosphorus and simultaneously remove heavy metals. The present work is an experimental screening of different options for ED in relation to experimental setup and combination with acid addition. Experiments for stirred ash suspensions utilizing a three compartment cell setup where the anode, cathode and stirred suspension are separated by ion exchange membranes are reported. Simplifying this experimental setup by removing the anion exchange membrane brings the anode in direct contact with the stirred ash suspension. Through this adjustment, half-reactions at the anode contribute to the acidity of the stirred suspension resulting in increased dissolution of both phosphorus and heavy metals (Cd, Cu, Cr, Pb, Zn, Ni) and better separation of most heavy metals from the stirred ash suspension. When the ash is suspended in an acidic solution, these effects increase significantly in early stages of the experiments. The combination of ED in a two compartment setup and initial acidification of the stirred suspension is most effective in dissolving of phosphorus and separation of heavy metals. In this setup, up to 96% of the phosphorus in the ash was dissolved after 7 d. Using the three compartment setup and initially suspending the ash in distilled water, resulted in 53% dissolution of the total recovered phosphorus after 7 d. | |
| 04/01/2015 00:00:00 | |
| Link to Article | |
| 3.2.4 | Electrokinetic |
| Effective removal of Cd2+ and Pb2+ pollutants from wastewater by dielectrophoresis-assisted adsorption | |
| Dielectrophoresis (DEP) was combined with adsorption (ADS) to simultaneously and effectively remove Cd2+ and Pb2+ species from aqueous solution. To implement the process, bentonite particles of submicro-meter size were used to first adsorb the heavy metal ions. These particles were subsequently trapped and removed by DEP. The effects of the adsorbent dosage, DEP cell voltage and the capture pool numbers on the removal rate were investigated in batch processes, which allowed us to determine the optimal experimental conditions. The high removal efficiency, 97.3% and 99.9% for Cd2+ and Pb2+, respectively, were achieved when the ions are coexisting in the system. The microstructure of bentonite particles before and after ADS/DEP was examined by scanning electron microscopy. Our results suggest that the dielectrophoresis-assisted adsorption method has a high capability to remove the heavy metals from wastewater. Open image in new window | |
| 04/01/2019 00:00:00 | |
| Link to Article | |
| 3.2.5 | Electrokinetic |
| Heavy metal removal from sewage sludge under citric acid and electroosmotic leaching processes | |
| Abstract The heavy metals present in sludge are very harmful to the environment and the human body. It is necessary to remove them before sludge disposal. In this study, an ex situ method for removing heavy metals from sludge using electroosmosis was designed, and experiments were conducted to study the effects of electroosmosis voltages (30 V, 40 V and 50 V), citric acid concentrations (0.03 mol/kg, 0.06 mol/kg, 0.09 mol/kg and 0.12 mol/kg) and the power supply (continuous and interrupted) on the removal rate of heavy metals (Cu, Cr, Cd, Zn and Pb). The study found that the combination of the citric acid pretreatment and electroosmosis can effectively improve the removal rate of heavy metals. An appropriate increase in the voltage and citric acid concentration can improve the removal rate of heavy metals. The best combination was determined to be 40 V and 0.09 mol/kg. Under these conditions, the removal rates of Cu, Cr, Cd, Zn and Pb, were 14.39–41.28% (continuous power supply) and 21.78–42.36% (interrupted power supply). The interrupted power supply effectively improved the removal rates of Cd and Zn but reduced the removal rates of Cr and Pb. The power supply mode had no significant effect on the removal rate of Cu. Heavy metal speciation was analyzed by the BCR method, and the relationship between the ratio of easily removed metal speciation and the removal rate was studied. The increase in the ratio of easily removed speciation was accompanied by an increase in the removal rate, indicating that citric acid and electroosmosis increased the removal rate by increasing the ratio of easily removed speciation. However, the high pH value around the cathode caused by the electrochemical reaction was not conducive to the removal of heavy metals. | |
| 07/01/2020 00:00:00 | |
| Link to Article | |
| 3.2.6 | Electrokinetic |
| Potential Electrokinetic Remediation Technologies of Laboratory Scale into Field Application- Methodology Overview | |
| Heavy metal in soil possesses high contribution towards soil contamination which causes to unbalance ecosystem. There are many ways and procedures to make the electrokinetic remediation (EKR) method to be efficient, effective, and potential as a low cost soil treatment. Electrode compartment for electrolyte is expected to treat the contaminated soil through electromigration and enhance metal ions movement. The electrokinetic is applicable for many approaches such as electrokinetic remediation (EKR), electrokinetic stabilization (EKS), electrokinetic bioremediation and many more. This paper presents a critical review on comparison of laboratory scale between EKR, EKS and EK bioremediation treatment by removing the heavy metal contaminants. It is expected to propose one framework of contaminated soil mapping. Electrical Resistivity Method (ERM) is one of famous indirect geophysical tools for surface mapping and subsurface profiling. Hence, ERM is used to mapping the migration of heavy metal ions by electrokinetic. | |
| 04/01/2018 00:00:00 | |
| Link to Article | |
3.3 Electrocoagulation
Electrocoagulation (EC), is a technique used for wastewater treatment, wash water treatment, industrial processed water, and medical treatment. Electrocoagulation has become a rapidly growing area of wastewater treatment due to its ability to remove contaminants that are generally more difficult to remove by filtration or chemical treatment systems, such as emulsified oil, total petroleum hydrocarbons, refractory organics, suspended solids, and heavy metals.[\[Wiki\]](https://en.wikipedia.org/wiki/Electrocoagulation)
**Highlights:**
* Heavy metals have frequently been detected in metal plating wastewater. **In this study, electrocoagulation method using iron (Fe) and aluminum (Al) electrodes was applied to simultaneously remove four heavy metals (Cu, Ni, Zn, Cr) in artificial metal plating wastewater.** In electrocoagulation experiments using Fe electrodes, the mass of sludge formed was 0.68–2.50 kg/m3 and the amount of energy consumed was 0.37–2.78 kW h/m3, respectively, during the treatment of artificial metal plating wastewater containing four heavy metals in the absence of cyanide, which increased to 3.64–4.74 kg/m3 and 4.80–5.04 kW h/m3 for artificial wastewater in the presence of cyanide. [\[Art. #ARTNUM\]](#article-96077-2995529317)
* Inspired by the wastewater treatment in such industries as those of textiles, food, and petrochemistry, in the present work, electrocoagulation (EC) is applied for the first time to explore its feasibility in the treatment of wastewater with an initial COD of 424.29 mg/L from a Pb/Zn sulfide mineral flotation plant and its effect on water reuse. Typical parameters, such as anode materials, current density, initial pH, and additives, were characterized to evaluate the performance of the EC method. This study confirmed that EC is a promising method for the treatment and reuse of high-COD-containing wastewater in the mining industry, and it possesses great potential for wide industrial applications.[\[Paper\]](https://www.mdpi.com/2073-4441/12/2/595)
* Electrocoagulation is an electrochemical technique with many applications. This process has recently attracted attention as a potential technique for treating industrial wastewater due to its versatility and environmental compatibility. This process has been applied for the treatment of many kinds of wastewater such as landfill leachate, restaurant, carwash, slaughterhouse, textile, laundry, tannery, petroleum refinery wastewater and for removal of bacteria, arsenic, fluoride, pesticides and heavy metals from aqueous environments. The objective of the present manuscript is to review the potential of electrocoagulation process for the treatment of domestic, industrial and agricultural effluents, especially removal of heavy metals from aqueous environments.[\[Paper\]](https://link.springer.com/article/10.1186/s40201-015-0233-8)
| 3.3.1 | Electrocoagulation |
|---|---|
| Application of Electrocoagulation and Electrolysis on the Precipitation of Heavy Metals and Particulate Solids in Washwater from the Soil Washing | |
| Soil washing, ex situ mechanical technique, is one of the few permanent treatment alternatives to remove metal contaminants from soils by employing physical separation based on mineral processing technologies to remove discrete particles or metal-bearing particles and/or chemical extraction based on leaching or dissolving process to extract the metals from the soils into an aqueous solution. However, washwater remained from soil washing process contains discrete particulate particles along with heavy metals as solution phase to be treated separately, as well as this process can produce large amount of sludge that requires further treatment, slow metal precipitation, poor settling, the aggregation of metal precipitates. Electrical treatments including electrocoagulation and electrolysis can be effective in removing these substances from washwater. This paper reviews the theoretical models in applying electrocoagulation and electrolysis to remove heavy metals and discrete particulate particles in washwater by examining and comparing the status of washwater treatment technologies which have been undertaken, mostly in the US and EU for the period 1990-2012. | |
| 01/01/2014 00:00:00 | |
| Link to Article | |
| 3.3.2 | Electrocoagulation |
| Removal mechanism of heavy metal (Cu, Ni, Zn, and Cr) in the presence of cyanide during electrocoagulation using Fe and Al electrodes | |
| Abstract Heavy metals have frequently been detected in metal plating wastewater. In this study, electrocoagulation method using iron (Fe) and aluminum (Al) electrodes was applied to simultaneously remove four heavy metals (Cu, Ni, Zn, Cr) in artificial metal plating wastewater. The Fe electrode showed greater removal efficiency for especially Cr than did the Al electrode due to the reduction of Cr6+ ion by Fe2+ ions produced from electrode. Alkaline pH favored electrocoagulation because of the abundance of hydroxide (OH−) ions; thus, metal hydroxides can be formed readily under alkaline pH. The metal removal increased with current density, as Fe2+ ion was generated more effectively at high current. However, the electrolyte concentration did not significantly affect metal removal efficiency. In electrocoagulation experiments using Fe electrodes, the mass of sludge formed was 0.68–2.50 kg/m3 and the amount of energy consumed was 0.37–2.78 kW h/m3, respectively, during the treatment of artificial metal plating wastewater containing four heavy metals in the absence of cyanide, which increased to 3.64–4.74 kg/m3 and 4.80–5.04 kW h/m3 for artificial wastewater in the presence of cyanide. The FTIR spectra of the sludge samples generated when using Fe and Al electrodes showed that all four metals exhibited OH stretching peaks, implying that main removal mechanism of metals during electrocoagulation is the precipitation with metal hydroxide. Iron sludge was composed mainly of Fe3O4 and FeO(OH), and Al sludge was mostly AlO(OH). When using Fe electrode in the presence of cyanide, cyanide was also adsorbed onto iron sludge via Fe-CN bonding. | |
| 02/01/2020 00:00:00 | |
| Link to Article | |
| 3.3.3 | Electrocoagulation |
| The innovative use of electrocoagulation-microwave techniques for the removal of pollutants from water | |
| Electrocoagulation (EC) is an effective water and wastewater treatment technology; where the coagulants are generated in-situ by electrolytic oxidation of a sacrificial anode. In this technique, pollutant removal is done without adding chemicals; therefore, it remarkably reduces the sludge produced, and consequently reduces the cost of sludge handling. This method has been efficiently used to remove, up to 99%, of a wide range of pollutants such as heavy metals, oil, dyes, and fluoride. However, the EC technology still has a deficiency in the variety of reactor design, and its performance is highly influenced by the chemistry of the water being treated, especially the presence of organic matter (OM), as this inhibits heavy metal removal due to the formation OM-heavy metals complexes. The presence of heavy metals and OM in water resources is one of the most problematic pollutants in Hilla River, Babylon city, Iraq, which inhibits the application of the EC method in that area. Thus, the current study has been devoted to develop a new hybrid EC rector that can be applied to treat water drawn from Hilla River especially, and to treat water containing OM-heavy metals complexes. The aims of this study are therefore; firstly to examine the removal of heavy metals from drinking water in the presence of OM-heavy metal complexes using a new hybrid treatment method that utilises a combination of microwave-electrocoagulation (MW assisted-EC method). Secondly, to present a new configuration for an electrocoagulation reactor (FCER) that employs perforated plate flow columns (which are widely used in the chemical industry) to achieve water mixing, aeration, and temperature control processes. Additionally, the development of statistical models for the EC performance, recovery of hydrogen gas, and the removal of biological pollutants are other targets in the present project. Initially, the performance of the new flow column EC reactor (FCER) was validated in terms of water mixing efficiency, water aeration, and temperature controllability. The results were compared to those of traditional EC reactors. Then, the ability of the FCER to work as an EC unit was validated by treating different pollutants such as fluoride, nitrate, iron, and reactive black 5 (RB-5) dye from drinking water. Then, the ability of the new MW assisted-EC method to remove OM-heavy metal complexes was experimentally proved by treating synthetic water samples contain iron (Fe2+) ions and ethylenediaminetetraacetic acid (EDTA) (C10H16N2O8) (as organic matter). The results obtained showed that FCER achieved a complete water mixing efficiency, and increased the dissolved oxygen (DO) concentration by 110.6% within 10 min, and kept the temperature of water being treated within the range of 22-28 oC for 30 min of electrolysing. While the traditional reactors achieved water-mixing efficiency of 96.5%, increased the DO by 52.2%, and the temperature increased to about 32 oC over the same treatment period. Additionally, FCER was able to reduce fluoride, iron, nitrate, and RB-5 dye concentrations by 98%, 99.6%, 95.2%, 98.6%, respectively. In terms of OM-heavy metal complex removal (the novelty of the present work), the results obtained demonstrated that this novel method removes 92% of this refractory complex within 35 min of treatment at a power of 100 W, temperature of 100 oC, initial pH of 6, ID of 5 mm, and CD of 1.5 mA/cm2. While, the traditional treatment (EC only) removed only 69.6% of this complex under the same operating conditions. It is noteworthy to mention, the new MW assisted-EC method achieved 100% removal of culture-able activated sludge microorganisms ASM from drinking water, which could eliminate the need for costly separated biological treatment units. Statistically, empirical models were developed to reproduce the performance of FCER in terms of fluoride, nitrate, RB-5 dye, iron, and iron-EDTA complex removal. The R2 value for the models of fluoride, nitrate, RB-5 dye, iron, and iron-EDTA complex removal were, respectively, 0.823, 0.848, 0.798, 0.868, and 0.923. Economically, it has been found that the preliminary operating cost of the MW assisted-EC method is 0.628 US $/m3. Additionally, it has been found that the generated hydrogen gas from this new method could be used to reproduce about 2.82 kW/m3 of power, which is a promising amount of power on field scale plants. In conclusion, according to the obtained results, the new MW assisted-EC method is a safe promising alternative to the complicated, expensive, and time consuming traditional treatment methods, as it removes heavy metals in the presence of OM in a relatively short time without the need for chemical additives. Economically, the MW assisted-EC method reduces the need for separated biological treatment unit that require space, money, equipment, and time, because drinking water will be sterilised as it passes through the microwave field. The latter merit makes this new method a cost-effective alternative. Additionally, FCER reduces the need for external mixing and aeration devices that require extra power to work, which makes FCER a cost-effective alternative for traditional lab-scale EC units. | |
| 01/01/2017 00:00:00 | |
| Link to Article | |
3.4 Electroflotation
***Electroflotation*** is a process of floating of pollutants to water surface by tiny bubbles of hydrogen and oxygen gases generated from water electrolysis.
**Highlights:**
* Electro-flotation is a removal process which produced tiny bubbles of hydrogen and oxygen gases emerged from water electrolysis to float the contaminants at the surface of effluent. The electro-flotation process can be used with the combination of aluminium electrocoagulation. This process was employed for the remediation of Ni(II) from the polymetallic solution. The removal efficiency was obtained 99% at the pH of 8.0. [\[Paper\]](https://www.researchgate.net/publication/331952883_Remediation_of_Nickel_ion_from_wastewater_by_applying_various_techniques_a_review)
* Flotation is a known gravity separation process originated from mineral processing; concerning the used bubble generation method, this could be typically by dispersed-air flotation, dissolved-air flotation or electroflotation. The later technique constitutes the scope of the present review article, commenting recent selected papers published in the literature, and focusing on applications such as waters, heavy metals, biological wastes, etc. Examples given (from our lab) are, among others, minerals like magnesite and pyrite, and pollutant metal ions, as Cd(II) and Cr(VI). The process advantages were discussed in-depth, such as the electric field gradient and the fine gas bubbles; and also, certain design aspects (as kinetics, hydrodynamics, electrolytic cell). Electroflotation was shown to contribute well for the recycling of by-products and waste materials, including water.[\[Paper\]](https://www.sciencedirect.com/science/article/abs/pii/S0167732216301660)
3.5 Electro-deionization
Electro-deionization is the combination of ion exchange and electrodialysis. It is often used as a polishing step.
**Highlights:**
* Dermentzis et al. employed an electro-deionization method for the removal of nickel from electroplating rinse water. The removal efficiency was obtained 100% at pH 4.0 by using platinum graphite powder platinum as an anode and platinum platinized titanium platinum as a cathode. The initial concentration of nickel was 0.1 mg/L at the flow rate of 2.02 x 10-4 and the current density was 30 A/m2.
* In this work, the treatability of nickel containing wastewater by membrane-free electrodeionization (MFEDI) was experimentally investigated. The study concentrated on the effect of different resin bed configurations in MFEDI system in term of nickel removal, precipitation generation and water recovery, as well as energy consumption. The experiment results show that excellent purification and effective regeneration were achieved by MFEDI with a layered mixed bed. It was observed that, in the purification stage, with an inlet conductivity of 42.5 μS/cm and a nickel concentration of 10.0 mg/L, the effluent conductivity was 0.3–1.0 μS/cm and the nickel concentration of the effluent was below the detection limit. [\[Paper\]](https://www.sciencedirect.com/science/article/abs/pii/S1385894715009043)
3.6 Bioelectrochemical
bioelectrochemical systems (BES) have emerged as a potential technological platform for recovery of metal ions from metallurgical waste (end-of-life products), process streams and wastewaters. In bioelectrochemical systems, microbial oxidation of organic substrate at the anode is coupled to abiotic or biotic reduction of metal ions at the cathode.[\[Paper\]](https://link.springer.com/chapter/10.1007/978-3-319-58622-9_6)
**Highlights:**
* MFC technology arises as an attractive alternative for the treatment of high strength animal wastewater, such as pig slurries, to potentially improve energetic valorisation of organic wastes, **concomitantly to carbon and nitrogen content reduction or recovery**.[ \[Art. #ARTNUM\]](#article-96158-2202793691)
* the bioelectrochemical approach, which is based on the integration of microbiology with electrochemistry, is **emerging as a potential technology for the efficient removal or recovery of various metals. It offers a flexible platform based on the oxidation and reduction reactions of different heavy metals at the electrodes.** This chapter covers different aspects associated with the use of microbial (bio)electrochemical systems for the removal and recovery of various metals.[\[Paper\]](https://www.sciencedirect.com/science/article/pii/B9780128174937000035)
| 3.6.1 | Bioelectrochemical |
|---|---|
| Electro-fermentation of iron-enhanced primary sedimentation sludge in a two-chamber bioreactor for product separation and resource recovery | |
| Abstract Iron (Fe)-based chemically enhanced primary sedimentation (CEPS) is an effective process used to remove organic and phosphorus (P) pollutants from wastewater into sludge. In this study, electro-fermentation (EF) technology was developed to treat the organic- and P-rich Fe-sludge for the purposes of sludge reduction and resource recovery. Using a two-chamber bioreactor with a cation exchange membrane and an exterior voltage (0.5–1.0 V) for sludge treatment, the EF system enabled product accumulation and separation during the fermentation process. Compared with the conventional fermentation in a single-chamber reactor, the EF treatment of Fe-sludge significantly improved the efficiency of P dissolution from the sludge from 8% to 56% after 4 d. Meanwhile, about 70% of released ammonium ions and 50% of Fe in the sludge were driven by the current from the sludge suspension into the cathode chamber for potential recovery. With a similar yield of volatile fatty acids (VFAs) but less ammonium remaining, the COD VFA /N NH4 of the sludge supernatant from the EF reactor could reach 67.7, much higher than that from the single-chamber fermenter at 13.0. The protease activity was effectively promoted by the EF treatment, suggesting that both electrochemical and biological hydrolysis effects contributed to the increased P release from the sludge. Microbial community analysis showed that the electrical stimulation increased the relative abundance of Firmicutes and facilitated the growth of Acidobacteria . Overall, electro-fermentation was developed as an effective biotechnology for processing Fe-based CEPS sludge with the benefits of recovering organics, phosphorus, ammonium and iron resources. | |
| 06/01/2019 00:00:00 | |
| Link to Article | |
| 3.6.2 | Bioelectrochemical |
| Microbial fuel cell running on high strength animal wastewater : nitrogen removal strategies and microbial community characterization | |
| A microbial fuel cell (MFC) is a bioelectrochemical system (BES) capable of converting the chemical energy contained in the chemical bonds of a substrate into electrical energy by means of electrochemical reactions catalyzed by microorganisms. The amount of energy to be gained by bacteria capable of transferring electrons to an anode is significantly higher compared to other alternative electron acceptors. Exoelectrogenic microbial populations tend to be selectively enriched on the anode electrode, being essential for the performance improvement of the MFC in terms of electricity production from organic matter oxidation. MFC technology arises as an attractive alternative for the treatment of high strength animal wastewater, such as pig slurries, to potentially improve energetic valorisation of organic wastes, concomitantly to carbon and nitrogen content reduction or recovery. The first part of the thesis (Chapters 4, 5 and 6) focuses on the study of microbial populations harboured on the anode electrode of MFCs. The effect of different ion exchange membrane materials and different inoculum sources over the microbial population was studied in discontinuously fed MFCs. A detailed study of the microbial community dynamics and composition onto the anode biofilms, under different feeding conditions (synthetic wastewater and the liquid fraction of pig slurry), was then studied in continuously fed MFC. A highly diverse microbial community is shown to be present under these different scenarios and, its final composition is being dependent on the factors studied. The second part of the thesis is focused on understanding the nitrogen dynamics in a two-chambered MFC, and the possible strategies available to remove or recover it. First of all, the diffusion/migration of ammonia nitrogen through the cation exchange membrane was studied in batch essays under different operational conditions (Chapter 7). The results obtained showed that the diffusion/migration of ammonia nitrogen is dependent on the voltage applied and, when using pig slurry, ammonia migration reaches values close to 50%. These results suggested that the use of MFC technology could be a good strategy to deal with the nitrogen excess in this kind of substrates. Two different processes for MFC nitrogen recovery and removal were developed. First, a physicochemical-based process for nitrogen recovery was developed coupling a stripping-absorption unit to the cathode chamber (Chapter 7). Results showed the stripping/absorption-BES system is a feasible technology to recover ammonia from pig slurries. Second, a nitrogen removal strategy by means of biological processes was studied using synthetic high strength wastewater as feed (Chapter 8). In this case, the ammonia nitrogen migrating from the anode to the cathode, was removed applying intermittent aeration cycles in the cathode chamber of the MFC where a concomitant nitrifying-denitrifying microbial community being established. The feasibility to recover/remove nitrogen from high strength animal wastewater, such as pig slurries, using different MFC strategies has been demonstrated at lab scale. Hence, it can be considered as a potential technology for scaling up the treatment of high strength (organic and nitrogen) wastewaters, so as to accomplish the requirements needed for agricultural uses. Likewise, the knowledge acquired about the biofilm developed on the anode reveals itself as a key point for the resilience of BES at different environmental conditions and for further developments. | |
| 07/24/2015 00:00:00 | |
| Link to Article | |
4. Biological
BackBiological system for contaminant removal
4.1 Bioleaching
Bioleaching is the extraction of metals from their ores through the use of living organisms. [\[Wiki\]](https://en.wikipedia.org/wiki/Bioleaching)
It has also been developed for sludge treatment.
**Highlights:**
* Three kinds of mixed culture of acidophilic bacteria were enriched and prepared from natural acid mine drainage and used in bioleaching experiments.The heavy metals (Cu,Zn and Cd) removal f rom sewage sludge and the improvement of sewage sludge dewaterability in bioleaching processes were investigated.The results showed that all the three prepared mixed culture of acidophilic bacteria could efficiently remove heavy metals from sewage sludge(P0.01).After 12 days of bioleaching,82.0% of copper and 82.9% of Cd could be removed by the mixed culture of acidophilic bacteria enriched by modified Starkey medium,and 87.5% of zinc could be leached out when inoculating the mixed culture of acidophilic bacteria enriched by 9K medium. [\[Art. #ARTNUM\]](#article-96079-2359122416)
* The bioleaching process, although it seems to give a higher yield of metal extraction with lower chemical cost than chemical extraction, may be limited by the inability of the system to cope with the natural environmental conditions, requires strict monitoring of aeration rate and temperature and has applicability to only low sludge solids concentration. [\[Art. #ARTNUM\]](#article-96079-2140127378)
* The purpose of this work was to study the sulfur concentration on bioleaching of heavy metals from pig manure employing indigenous sulfur-oxidizing bacteria. Also, the variations in physicochemical properties of pig manure before and after bioleaching were investigated. The results showed that sulfur concentration significantly affected the rate of acidification, sulfate production and metal solubilization during pig manure bioleaching process. After 12 days of bioleaching, 93%–97% of Zn, 96%–98% of Mn and 48%–94% of Cu were leached out from pig manure, respectively. [\[Paper\]](https://www.sciencedirect.com/science/article/pii/S2405844017339725#:\~:text=In%20the%20bioleaching%20process%2C%20the,efficiency%20during%20the%20bioleaching%20process.)
| 4.1.1 | Bioleaching |
|---|---|
| Advances in bioleaching for recovery of metals and bioremediation of fuel ash and sewage sludge | |
| Abstract Bioleaching has been successfully used in commercial metal mining for decades. It uses microbes to biosolubilize metal-containing inorganic compounds such as metal oxides and sulfides. There is a growing interest in using bioleaching for bioremediation of solid wastes by removing heavy metals from ash and sewage sludge. This review presents the state of the art in bioleaching research for recovery of metals and bioremediation of solid wastes. Various process parameters such as reaction time, pH, temperature, mass transfer rate, nutrient requirement, pulp density and particle size are discussed. Selections of more effective microbes are assessed. Pretreatment methods that enhance bioleaching are also discussed. Critical issues in bioreactor scale-up are analyzed. The potential impact of advances in biofilm and microbiome is explained. | |
| 08/01/2018 00:00:00 | |
| Link to Article | |
| 4.1.2 | Bioleaching |
| Bioleaching of heavy metals from sludge after biological treatment of municipal effluent | |
| The article has compared the efficiency of removing heavy metals from the sludge after biological treatment of municipal wastewaters in the course of biological leaching involving heterotrophic and chemotrophic microorganisms and chemical leaching. The article also showed advantages of the bioleaching of metals under conditions of acidogenic heterotrophic metabolism. The efficiency of the leaching of heavy metals from the sludge varies 80% (Zn) to 15% (Cr) and corresponds to the following series: Zn > Mn > Cu > Ni > Cd > Pb > Cr. | |
| 03/01/2013 00:00:00 | |
| Link to Article | |
| 4.1.3 | Bioleaching |
| Bioleaching remediation of heavy metal-contaminated soils using Burkholderia sp. Z-90 | |
| Bioleaching is an environment-friendly and economical technology to remove heavy metals from contaminated soils. In this study, a biosurfactant-producing strain with capacity of alkaline production was isolated from cafeteria sewer sludge and its capability for removing Zn, Pb, Mn, Cd, Cu, and As was investigated. Phylogenetic analysis using 16S rDNA gene sequences confirmed that the strain belonged to Burkholderia sp. and named as Z-90. The biosurfactant was glycolipid confirmed by thin layer chromatography and Fourier-transform infrared spectroscopy. Z-90 broth was then used for bioleaching remediation of heavy metal-contaminated soils. The removal efficiency was 44.0% for Zn, 32.5% for Pb, 52.2% for Mn, 37.7% for Cd, 24.1% for Cu and 31.6% for As, respectively. Mn, Zn and Cd were more easily removed from soil than Cu, Pb and As, which was attributed to the presence of high acid-soluble fraction of Mn, Zn and Cd and high residual fraction of Cu, Pb and As. The heavy metal removal in soils was contributed to the adhesion of heavy metal-contaminated soil minerals with strain Z-90 and the formation of a metal complex with biosurfactant. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 4.1.4 | Bioleaching |
| Comparison of bioleaching and electrokinetic remediation processes for removal of heavy metals from wastewater treatment sludge | |
| Abstract Heavy metals prevent the growing amount of sewage sludge from being disposed as fertilizeron land. The electrokinetic remediation and bioleaching technology are the promising methods to remove heavy metals. In recent years, some innovation has been made to achieve better efficiency, including the innovation of processes and agents. This paper reviews the development of the electrokinetic remediation and bioleaching technology and analyses their advantages and limitation, pointing out the need of the future research for the heavy metals-contaminated sewage sludge. | |
| 02/01/2017 00:00:00 | |
| Link to Article | |
| 4.1.5 | Bioleaching |
| Decontamination of heavy metal laden sewage sludge with simultaneous solids reduction using thermophilic sulfur and ferrous oxidizing species | |
| A possibility of using simultaneous sewage sludge digestion and metal leaching (SSDML) process at the thermophilic temperature to remove heavy metals and suspended solids from sewage sludge is explored in this study. Though thermophilic sludge digestion efficiently produces a stable sludge, its inability to remove heavy metals requires it to be used in tandem with another process like bioleaching for metal reduction. Previously, different temperature optima were known for the heterotrophs (thermophilic) responsible for the sludge digestion and the autotrophs involved in bioleaching (mesophilic), because of which the metal concentration was brought down separately in a different reactor. In our study, SSDML process was carried out at 50 °C (thermophilic) by using ferrous sulfate (batch-1) and sulfur (batch-2) as the energy source in two reactors. The concentration of volatile suspended solids reduced by >40% in both batches, while that of heavy metals zinc, copper, chromium, cadmium and nickel decreased by >50% in both batch-1 and batch-2. Lead got leached out only in batch-1. Using 16S rRNA gene-based PCR-denaturing gradient gel electrophoresis analysis, Alicyclobacillus tolerans was found to be the microorganism responsible for lowering the pH in both the reactors at thermophilic temperature. The indicator organism count was also below the maximum permissible limit making sludge suitable for agricultural use. Our results indicate that SSDML at thermophilic temperature can be effectively used for reduction of heavy metals and suspended solids from sewage sludge. | |
| 02/01/2016 00:00:00 | |
| Link to Article | |
| 4.1.6 | Bioleaching |
| Environment-enhancing process for algal wastewater treatment, heavy metal control and hydrothermal biofuel production: A critical review | |
| Abstract Coupling algae growth on wastewater with hydrothermal liquefaction (HTL) is regarded as an environment-enhancing pathway for wastewater management, biomass amplification, sustainable energy generation and value-added products generation. Through this integrated pathway, microalgae can not only recover nitrogen and phosphorus, but also absorb heavy metals from the wastewater. The migration and transformation of heavy metals need to be specifically assessed and considered due to the environmental concerns associated with metal toxicity. This work reviewed recent advances with respect to bioremediation mechanisms. Particular emphasis was placed on the heavy metal migration, transformation, and the key factors involved in algal wastewater treatment and biomass conversion. Additionally, the challenges of coupling algae wastewater treatment, hydrothermal conversion, and heavy metal control were addressed. Finally, a paradigm involving enhanced algal wastewater treatment and bioenergy production for field application was proposed. | |
| 11/01/2019 00:00:00 | |
| Link to Article | |
| 4.1.7 | Bioleaching |
| Evaluation of microalgae’s (Chlorella sp. and Synechocystis sp.) pollutant removal property: Pig effluent as a live stock discharge - | |
| The ability of microalgae to remove nitrogen and phosphorus from wastewater has been used in recent years as an alternative treatment for discharges from livestock slurry, which generate a negative environmental impact on vulnerable ecosystems. With this background and the feasibility of using microalgae, we have evaluated the effect of Chlorella sp. and Synechocystis sp., in removing contaminants from the pig manure collected from El Prado ESPE. Slurry samples were collected, filtered and autoclaved, and the supernatant was further dilluted to three different concentrations of 40%, 60% and 80%. The microalgal growth and pollutants removal property was evaluated up to 15 days in batch culture. The cell density was determined by counting in a Neubauer hemocytometer, and the pollutants removal was analyzed by standard colorimetric methods. The microalgae Chlorella sp. showed a maximum cell growth of 1.70 ± 0.09 x107 cells/mL at 60% effluent concentration on day 6. While Synechocystis sp. showed a maximum growth of 1.04 ± 0.05 x107 cells/mL, at 60% concentration on day 9. On the other hand, there exists a competition when microalgae used as a consortium. The cell growth of Chlorella sp. was higher at all concentrations compared to Synechocystis sp.. Overall, efficiency of pollutant removal were between 40% and 90%, which demonstrate the feasibility of using microalgae in tertiary swine wastewater treatment. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 4.1.8 | Bioleaching |
| Heavy metal removal from contaminated sludge for land application : A review | |
| In recent years, various methods for heavy metal removal from sewage sludge have been extensively studied in order to minimize the prospective health risks of sludge during land application. In this paper, a comparative review and critical analysis of the application of chemical extraction, bioleaching, electroreclamation, and supercritical fluid extraction (SFE), in removing heavy metals from contaminated sludges is presented. Moreover, speciation studies, which can indicate ease of leachability of the different forms of heavy metals in sludge, are also presented. Experimental studies revealed a broad range in metal extraction efficiencies of the different extraction technologies. Acid treatment seemed to effectively remove Cd, attaining as much as 100% removal for some studies, as compared to bioleaching. SFE also gave higher removal efficiency than bioleaching. Cr, Pb and Ni seemed to be also effectively removed by the acid treatment. For the removal of Cu, Mn and Zn, the bioleaching process seemed to be appropriate with maximum removal efficiencies of 91%, 93% and 96% for the three metals, respectively, and as high as 64% minimum removal efficiency for Zn. The SFE process also gave good results for Cu, Mn and Zn removal. Electroreclamation exhibited better removal efficiency for Mn, but is still inferior to acid treatment and bioleaching processes. For chemical extraction, because of the adverse impacts that can result from the use of inorganic acids and complexing agents, interest can be directed more toward utilizing organic acids as extracting agents because of their biodegradability and capability to remove metals at mildly acidic condition, hence requiring less acid. The bioleaching process, although it seems to give a higher yield of metal extraction with lower chemical cost than chemical extraction, may be limited by the inability of the system to cope with the natural environmental conditions, requires strict monitoring of aeration rate and temperature and has applicability to only low sludge solids concentration. A full-scale study would be useful to better assess the efficiency of the process. The electroreclamation technology is limited by its relatively higher energy consumption and limited applicability to sludge. The SFE method, on the other hand, is limited by the complexity of the process and the cost of ligands suitable for effective metal extraction. Both of these technologies are still in their early stage of application and hence there is a need for further basic and applied studies. Finally, the common advantage for almost all treatment technologies studied is that the extraction efficiencies for some metals are high enough to remove metals from sludge to levels suitable for land application. | |
| 01/01/2006 00:00:00 | |
| Link to Article | |
| 4.1.9 | Bioleaching |
| Heavy metals removal from sewage sludge and dewaterability improvement by bioleaching | |
| Three kinds of mixed culture of acidophilic bacteria were enriched and prepared from natural acid mine drainage and used in bioleaching experiments.The heavy metals(Cu,Zn and Cd) removal from sewage sludge and the improvement of sewage sludge dewaterability in bioleaching processes were investigated.The results showed that all the three prepared mixed culture of acidophilic bacteria could efficiently remove heavy metals from sewage sludge(P0.01).After 12 days of bioleaching,82.0% of copper and 82.9% of Cd could be removed by the mixed culture of acidophilic bacteria enriched by modified Starkey medium,and 87.5% of zinc could be leached out when inoculating the mixed culture of acidophilic bacteria enriched by 9K medium.Meanwhile,the bioleaching processes could also significantly enhance sewage sludge dewaterability(P0.01).The centrifugal dehydration efficiency of sewage sludge rose from 73.1% up to 90.0% after 12 days of bioleaching.The microscope observation and energy spectrum analysis demonstrated that the dewaterability improvement of sewage sludge was attributable to the changes of particle structure from flocculent to obvious granular and the formation of the secondary minerals mainly consisting of iron,oxygen and sulfur elements in the bioleaching processes. | |
| 01/01/2013 00:00:00 | |
| Link to Article | |
| 4.1.10 | Bioleaching |
| Phosphorus recovery from sewage sludge ash with bioleaching and electrodialysis | |
| Abstract Phosphorus is an essential element for all living organisms and for plants. However, phosphate rock, which is the main source of phosphorus, is limited and thus it must be recovered from secondary sources like sewage sludge ash (SSA). SSA is one of the most promising secondary sources because it contains considerable amounts of phosphorus. The drawback of SSA as a secondary source is the presence of heavy metals along with phosphorus. In this study, a bioleaching process was applied to solubilize the phosphorus more economically, thus bioleaching bacteria was used to obtain acidic conditions for phosphorus leaching. For this purpose, batch bioleaching experiments were carried out with Sulfur oxidizing bacteria (SOB) to optimize the process in terms of phosphorus dissolution. Experiments were conducted with different amounts of ash, inoculum volumes, and sulfur concentrations. Because the application of the bioleaching process leads to solubilization of heavy metals beside phosphorus, an electrodialysis process was used to separate phosphorus from heavy metals. Electrodialysis experiments were performed in a 3 compartment electrodialysis reactor with gold coated copper electrodes. The maximum phosphorus bioleaching was obtained with 2 g of ash, 40% inoculum, and 10 g.l-1 elemental sulfur. Electrodialysis studies with gold coated copper electrodes lasted for 14 days and 24.6% of the phosphorus was transported to the anode. | |
| 10/01/2019 00:00:00 | |
| Link to Article | |
| 4.1.11 | Bioleaching |
| Removal of Heavy Metals from Sewage Sludge by Bioleaching | |
| This study aims to evaluate the bioleaching process to remove heavy metals from sewage sludge.Sludge acclimatization and bioleaching are both performed on sewage sludge collected from one wastewater treatment plant of Guangzhou. Different sludge inoculation(5%,10%,20%)is added in the treated sludge to study the removal efficiency of heavy metals(Zn,Cd,Pb,Cu).The results show that with the inoculation of 5% of the cultivated sludge,the removal rate of Zn,Cd,Cu and Pb is 46%,54.6%,13.9% and 30.5% respectively,but that of Zn,Cd, Cu and Pb can reach 72%,79.6%,29% and 65.4% respectively.The cultivated sludge mixed liquid had better removal efficiency on heavy metals Zn,Cd and Cu,but lower removal efficiency on Pb,highest only to 29%. | |
| 01/01/2013 00:00:00 | |
| Link to Article | |
4.2 Bioleaching hybrid technologies
These examples combine bioleaching with different technologies: advanced oxidation, filtration, electro-techniques.
**Highlights:**
* Feasibility of **bioleaching combining with Fenton-like reaction** to remove heavy metals from sewage sludge was investigated. After 5-day bioleaching, the sludge pH decreased from 6.95 to 2.50, which satisfied the acidic conditions for Fenton-like reaction. Meanwhile, more than 50% of sludge-borne heavy metals were dissolved except for Pb. The bioleached sludge was further oxidized with Fenton-like reaction, with an optimal H2O2 dosage of 5 g/L, the Cu, Zn, Pb and Cd removal reached up to 75.3%, 72.6%, 34.5% and 65.4%, respectively, and the residual content of heavy metals in treated sludge meets the requirement of Disposal of Sludge from Municipal Wastewater Treatment Plant – Control Standards for Agricultural Use (CJ/T 309-2009) of China for A grade sludge. Bioleaching combined with Fenton-like reaction was the most effective method for heavy metal removal, compared with 15-day bioleaching and inorganic acid leaching with 10% H2SO4, 10% HCl and 10% HNO3. [\[Art. #ARTNUM\]](#article-96090-1979915077)
* The combination of **bioleaching and electrokinetic** remediation has been proved to be an effective method to remove heavy metals from municipal sewage sludge. The results showed that using electrokinetic remediation for six days after bioleaching for four days, the contents of Cu and Zn in sewage sludge decreased from 296.4 mg kg − 1 and 3756.2 mg kg − 1 to 63.4 mg kg − 1 and 33.3 mg kg − 1 , respectively, which could meet the Chinese standard for land application of the heavy metals in sewage sludge. [\[Art. #ARTNUM\]](#article-96090-2070246701)
* There is needed for treatment to remove chloride from wastewater before discharged to river or water bodies. Furthermore, chloride is also a very corrosive agent, and elevated levels pose a threat to infrastructure, such as road beds, bridges, and industrial pipes. The effect caused by these hazardous pollutants and growing concerns to environmental issues led to remove chloride concentration from rare earth wastewater by using bioremediation hybrid with electrocoagulation system. The application of yeast in the wastewater treatment has potential in the treatment and reuse of wastes containing solids and high concentrations of salt, fat and antibiotics. The information obtained from this study is useful for scale up purpose in the rare earth industry that choose bioremediation hybrid with electrocoagulation system method to remove chloride concentration from rare earth wastewater. [\[Art. #ARTNUM\]](#article-96090-2963928864)
* Trickling filters (TFs) constitute a cost-effective post-treatment option, assuring low sludge production, low operational costs and maintenance simplicity compared to other post-treatment technologies (e.g. activated sludge). This paper reviews the experience of the last 20 years of research, design and operation of UASB/TF systems. Three main topics are addressed: i) the development of trickling filters for UASB reactor effluent treatment, building on first experiences with TFs preceded by primary settlers; ii) the design criteria, performance and empirical models for predicting the efficiency of TFs post-UASB reactors; and iii) the future challenges associated with elimination of secondary settlers and nitrogen removal in sponge-bed trickling filters (SBTFs). [\[Art. #ARTNUM\]](#article-96090-2892119691)
* A hybrid process (**coupling biological and chemical processes**) has been explored in laboratory pilot-scale experiments for heavy metals (cadmium \[Cd\], copper \[Cu\], chromium \[Cr\], and zinc \[Zn\]) removal from three types of sludge (primary sludge, secondary activated sludge, and a mixture of primary and secondary sludge). The hybrid process consisted of producing a concentrate ferric ion solution followed by chemical treatment of sludges. Ferric iron solution was produced biologically via oxidation of ferrous iron by A. ferrooxidans in a continuous-flow stirred tank (5.2 L) reactor (CSTR). Wastewater sludge filtrate (WSF) containing nutrients (phosphorus and nitrogen) has been used as culture media to support the growth and activity of indigenous iron-oxidizing bacteria. [\[Art. #ARTNUM\]](#article-96090-2412106185)
| 4.2.1 | Bioleaching hybrid technologies |
|---|---|
| Comparison of bioleaching and electrokinetic remediation processes for removal of heavy metals from wastewater treatment sludge | |
| Abstract Heavy metals prevent the growing amount of sewage sludge from being disposed as fertilizeron land. The electrokinetic remediation and bioleaching technology are the promising methods to remove heavy metals. In recent years, some innovation has been made to achieve better efficiency, including the innovation of processes and agents. This paper reviews the development of the electrokinetic remediation and bioleaching technology and analyses their advantages and limitation, pointing out the need of the future research for the heavy metals-contaminated sewage sludge. | |
| 02/01/2017 00:00:00 | |
| Link to Article | |
| 4.2.2 | Bioleaching hybrid technologies |
| Feasibility of bioleaching combined with Fenton-like reaction to remove heavy metals from sewage sludge | |
| Feasibility of bioleaching combining with Fenton-like reaction to remove heavy metals from sewage sludge was investigated. After 5-day bioleaching, the sludge pH decreased from 6.95 to 2.50, which satisfied the acidic conditions for Fenton-like reaction. Meanwhile, more than 50% of sludge-borne heavy metals were dissolved except for Pb. The bioleached sludge was further oxidized with Fenton-like reaction, with an optimal H2O2 dosage of 5 g/L, the Cu, Zn, Pb and Cd removal reached up to 75.3%, 72.6%, 34.5% and 65.4%, respectively, and the residual content of heavy metals in treated sludge meets the requirement of Disposal of Sludge from Municipal Wastewater Treatment Plant – Control Standards for Agricultural Use (CJ/T 309-2009) of China for A grade sludge. Bioleaching combined with Fenton-like reaction was the most effective method for heavy metal removal, compared with 15-day bioleaching and inorganic acid leaching with 10% H2SO4, 10% HCl and 10% HNO3. | |
| 08/01/2013 00:00:00 | |
| Link to Article | |
| 4.2.3 | Bioleaching hybrid technologies |
| Hybrid process for heavy metal removal from wastewater sludge. | |
| Bioleaching processes have been demonstrated to be effective technologies in removing heavy metals from wastewater sludge, but long hydraulic retention times are typically required to operate these bioprocesses. A hybrid process (coupling biological and chemical processes) has been explored in laboratory pilot-scale experiments for heavy metals (cadmium [Cd], copper [Cu], chromium [Cr], and zinc [Zn]) removal from three types of sludge (primary sludge, secondary activated sludge, and a mixture of primary and secondary sludge). The hybrid process consisted of producing a concentrate ferric ion solution followed by chemical treatment of sludges. Ferric iron solution was produced biologically via oxidation of ferrous iron by A. ferrooxidans in a continuous-flow stirred tank (5.2 L) reactor (CSTR). Wastewater sludge filtrate (WSF) containing nutrients (phosphorus and nitrogen) has been used as culture media to support the growth and activity of indigenous iron-oxidizing bacteria. Results showed that total organic carbon (TOC) concentrations of the culture media in excess of 235 mg/L were found to be inhibitory to bacterial growth. The oxidation rate increased as ferrous iron concentrations ranged from 10 to 40 g Fe 2- /L. The percentage of ferrous iron (Fe 2+ ) oxidized to ferric iron (Fe 3+ ) increased as the hydraulic retention time (HRT) increased from 12 to 48 h. Successful and complete Fe 2+ oxidation was recorded at a HRT of 48 h using 10 g Fe 2+ /L. Subsequently, ferric ion solution produced by A. ferrooxidans in sludge filtrate was used to solubilize heavy metals contained in wastewater sludge. The best solubilization was obtained with a mixture of primary and secondary sludge, demonstrating a removal efficiency of 63, 71, 49, and 80% for Cd, Cu, Cr, and Zn, respectively. | |
| 07/01/2005 00:00:00 | |
| Link to Article | |
| 4.2.4 | Bioleaching hybrid technologies |
| Removal of heavy metals from sewage sludge with a combination of bioleaching and electrokinetic remediation technology | |
| Abstract The combination of bioleaching and electrokinetic remediation has been proved to be an effective method to remove heavy metals from municipal sewage sludge. The results showed that using electrokinetic remediation for six days after bioleaching for four days, the contents of Cu and Zn in sewage sludge decreased from 296.4 mg kg − 1 and 3756.2 mg kg − 1 to 63.4 mg kg − 1 and 33.3 mg kg − 1 , respectively, which could meet the Chinese standard for land application of the heavy metals in sewage sludge. During the bioleaching process, both the organic sulfide fraction of Cu and the carbonate-bound and organic sulfide fractions of Zn transformed to soluble and ionic fractions which could easily migrate to the electrode zone and then accumulate there, Finally, the soluble and ionic fractions of these heavy metals could be disposed of or recycled expediently at the end of electrokinetic remediation. | |
| 04/01/2011 00:00:00 | |
| Link to Article | |
| 4.2.5 | Bioleaching hybrid technologies |
| Study the optimum parameter in chloride removal from rare earth wastewater industrial using bioremediation hybrid with electrocoagulation system | |
| Chloride (Cl-) is a major anion found in all natural waters. It occurs naturally and is also a relatively minor contaminant. Currently, a larger amount chloride (Cl) in wastewater was generated from rare earth industrial. Chloride is non-toxic to humans, however, it can bring harmful to some plants and aquatic. There is needed for treatment to remove chloride from wastewater before discharged to river or water bodies. Furthermore, chloride is also a very corrosive agent, and elevated levels pose a threat to infrastructure, such as road beds, bridges, and industrial pipes. The effect caused by these hazardous pollutants and growing concerns to environmental issues led to remove chloride concentration from rare earth wastewater by using bioremediation hybrid with electrocoagulation system. The application of yeast in the wastewater treatment has potential in the treatment and reuse of wastes containing solids and high concentrations of salt, fat and antibiotics. However, Electrocoagulation is a novel method in wastewater treatment especially in chloride removal and this emerging technology combines the functions and advantage of conventional methods such as coagulation, flotation, and electrochemistry in water and wastewater treatment. The treated rare earth wastewater was tested for its chloride (Cl-) concentration to determine the percentage of reduction by measured using spectrophotometer. Results shows S. cerivisiae cells grew and adapted well under condition 10 g/L NaCl in suitable nutrient medium. Yeast was able to growth in standard (10 hr), synthetic chloride (6 hr) and actual wastewater (6 hr) with OD increased from 0.8 to 2.4, 0.8 to 1.2 and 0.4 to 0.6 respectively. Besides that, the optimum yeast able to growth in standard pH 6 at first 9 hours with OD increased from 1.1 to 2.1. Thus, the samples directly treat by using electrocoagulation system. The result shows ferum plate able to remove chloride concentration which is 75.0 % removal at 5 minute and 2 Ampere. The information obtained from this study is useful for scale up purpose in the rare earth industry that choose bioremediation hybrid with electrocoagulation system method to remove chloride concentration from rare earth wastewater. | |
| 09/01/2018 00:00:00 | |
| Link to Article | |
| 4.2.6 | Bioleaching hybrid technologies |
| Trickling filters following anaerobic sewage treatment: state of the art and perspectives | |
| High-rate anaerobic treatment of sewage using upflow anaerobic sludge blanket (UASB) reactors is a consolidated technology in warm climate countries. Nevertheless, since anaerobic treatment only removes organic carbon, post-treatment is required to remove nitrogen, besides residual organic carbon. Trickling filters (TFs) constitute a cost-effective post-treatment option, assuring low sludge production, low operational costs and maintenance simplicity compared to other post-treatment technologies (e.g. activated sludge). This paper reviews the experience of the last 20 years of research, design and operation of UASB/TF systems. Three main topics are addressed: i) the development of trickling filters for UASB reactor effluent treatment, building on first experiences with TFs preceded by primary settlers; ii) the design criteria, performance and empirical models for predicting the efficiency of TFs post-UASB reactors; and iii) the future challenges associated with elimination of secondary settlers and nitrogen removal in sponge-bed trickling filters (SBTFs). | |
| 01/01/2018 00:00:00 | |
| Link to Article | |
4.3 Biogranulation
This study investigated nutrient removal characteristics and the related pathways in aerobic granular reactors using three pilot-scale granular sequencing batch reactors (GSBRs) treating wastewaters of diverse carbon and nutrient strength. The GSBRs were operated with alternating (AN/O/AX/O_SBR and AN/O_SBR) and purely-aerobic (O_SBR) operation modes. Mineral-rich aerobic granules with hydroxyapatite (HAp) core were cultivated in all the three GSBRs. The highest **nitrogen removal efficiency (75%)** was achieved in AN/O/AX/O_SBR and O_SBR and the lowest (22%) in AN/O_SBR, establishing a quasi-linear relationship with organic loading rate (OLR). **Phosphorus removal efficiencies of 55–63%** were achieved in the GSBRs despite different influent PO~4~–P concentrations. Heterotrophic nitrification and biologically-induced phosphate precipitation (BIPP) became the dominant nutrient depletion pathways, contributing 61–84% and 39–96% to overall ammonium nitrogen and phosphorus removal, respectively. Core heterotrophic nitrifiers and bio-calcifying species were identified as {*Thauera* and *Flavobacterium*} and {*Flavobacterium*, *Acinetobacter*, *Pseudomonas*, and *Corynebacterium*}, respectively. Ca–P crystallization was proposed to be via phosphate precipitation on calcite surfaces. Granulation mechanism was proposed as crystallization on bio-aggregates’ periphery and then crystal growth toward the core.[\[Art. #ARTNUM\]](#article-96701-2977918113)
| 4.3.1 | Biogranulation |
|---|---|
| Pilot-scale investigation on nutrient removal characteristics of mineral-rich aerobic granular sludge: Identification of uncommon mechanisms | |
| Abstract This study investigated nutrient removal characteristics and related pathways using three pilot-scale granular sequencing batch reactors (GSBRs) treating wastewaters of diverse carbon and nutrient strength. The GSBRs were operated with alternating (AN/O/AX/O_SBR and AN/O_SBR) and purely-aerobic (O_SBR) operation modes. Mineral-rich aerobic granules with hydroxyapatite (HAp) core were cultivated in all the three GSBRs. The highest nitrogen removal efficiency (75%) was achieved in AN/O/AX/O_SBR and O_SBR and the lowest (22%) in AN/O_SBR, establishing a quasi-linear relationship with organic loading rate (OLR). Phosphorus removal efficiencies of 55–63% were achieved in the GSBRs despite different influent PO4–P concentrations. Heterotrophic nitrification and biologically-induced phosphate precipitation (BIPP) became the dominant nutrient depletion pathways, contributing 61–84% and 39–96% to overall ammonium nitrogen and phosphorus removal, respectively. A direct relation was noted between heterotrophic nitrification efficiency (η Heterotrophic nitrification) and nutrient availability, as nitrification efficiencies of 18 and 64% were observed for COD:Ninf of 5 and 20 respectively. Whereas, BIPP efficiency (η BIPP) established inverse relations with (COD:P)inf and phosphorus concentration beyond microbial growth requirement. Core heterotrophic nitrifiers and bio-calcifying species were identified as {Thauera and Flavobacterium} and {Flavobacterium, Acinetobacter, Pseudomonas, and Corynebacterium}, respectively. Ca–P crystallization was proposed to be via phosphate precipitation on calcite surfaces. Granulation mechanism was proposed as crystallization on bio-aggregates’ periphery and then crystal growth toward the core. | |
| 01/01/2020 00:00:00 | |
| Link to Article | |
4.4 Vermiremediation
Vermiremediation is an earthworm-based bioremediation technology.
**Highlights:**
* This work presents the results of removing heavy metals from paper mill wastewater (PMS) sludge spiked with cow dung (CD) employing Eisenia fetida . A total of seven set-ups were prepared: CD (100 percent), PMS: CD (1:3), PMS:CD (1:2), PMS:CD (1:1), PMS (100 percent), PMS:CD (3:1) and PMS:CD (2:1) and changes in chemical parameters were observed for 60 days. Vermistabilization caused the significant decrease in the level of Cd (32–37 percent), Cr (47.3–80.9 percent), Cu (68.8–88.4 percent), and Pb (95.3–97.5 percent) and substantial increase in EC, total-N, available P and K at the end. At the end, the tissues of inoculated worms showed the high load (mg kg −1 , dry biomass) of Pb (8.81–9.69), Cd (2.31–2.71), Cr (20.7–35.9) and Cu (9.94–11.6), respectively which indicated bioaccumulation of metals by worms. The PMS:CD (2:1 and/or 3:1) appeared to be suitable waste mixture in terms of high metal removal and earthworm growth rates. Bioaccumulation, as quantified using BCF, was in the order: Cd>Cr>Pb>Cu. Results suggested vermiremediation as appropriate technology for bioremediation of heavy metals from PMS.[ \[Art. #ARTNUM\]](#article-96095-2117836668)
* Efficacy of vermi-transformation for metal partitioning and transformation from **Upflow Anaerobic Sludge Blanket (UASB)** and Activated Sludge (AS) was investigated. Sludge samples were mixed with cow dung (CD) in two combinations (1:1 (UASB/AS:CD)) & (2:1(UASB/AS: CD)). Fractionation study revealed that Zn, Cd & Pb were associated with reducible fractions, and Cr, Cu with oxidizable fractions. Higher removal efficiency for 1:1 (UASB/AS: CD) combination over 2:1 (UASB/AS: CD) implies the non-significant contribution of cow dung during the metal stabilization process. **After vermi-remediation, maximum metal removal was achieved at 1:1 ratio than 2:1 in AS. In UASB, 1:1 ratio worked better for Cr, Zn & Cd, whereas for Cu & Zn 2:1 ratio resulted in efficient removal.** [ \[Art. #ARTNUM\]](#article-96095-2911869462)
| 4.4.1 | Vermiremediation |
|---|---|
| Efficacy of vermitechnology integration with Upflow Anaerobic Sludge Blanket (UASB) and activated sludge for metal stabilization: A compliance study on fractionation and biosorption | |
| Abstract Efficacy of vermi-transformation for metal partitioning and transformation from Upflow Anaerobic Sludge Blanket (UASB) and Activated Sludge (AS) was investigated. Sludge samples were mixed with cow dung (CD) in two combinations (1:1 (UASB/AS:CD)) & (2:1(UASB/AS: CD)). Fractionation study revealed that Zn, Cd & Pb were associated with reducible fractions, and Cr, Cu with oxidizable fractions. Higher removal efficiency for 1:1 (UASB/AS: CD) combination over 2:1 (UASB/AS: CD) implies the non-significant contribution of cow dung during the metal stabilization process. After vermi-remediation, maximum metal removal was achieved at 1:1 ratio than 2:1 in AS. In UASB, 1:1 ratio worked better for Cr, Zn & Cd, whereas for Cu & Zn 2:1 ratio resulted in efficient removal. Overall for both AS and UASB, efficiency was found to be higher in 1:1 treatment ratio. The value of K d (Bio sorption) was highest in Cu followed by Cr, which indicates the closer association with the metal bound organic matter (R 2 ≥ 0.99). Based on the compliance study between two estimated sorption coefficients K d (Biosorption & Fractions), vermi-remediation was found to be effective for AS than UASB. Therefore, the obtained results clearly validate the feasibility of integration of vermi-remediation as a potential promising ecological techniques for removing metal contaminant from the wastewater. Further research is required to study the decontamination of emerging contaminants with such integrated technology, which have physico-chemical properties different than metal ions. | |
| 04/01/2019 00:00:00 | |
| Link to Article | |
| 4.4.2 | Vermiremediation |
| Vermiremediation of heavy metals in wastewater sludge from paper and pulp industry using earthworm Eisenia fetida | |
| Abstract This work presents the results of removing heavy metals from paper mill wastewater (PMS) sludge spiked with cow dung (CD) employing Eisenia fetida . A total of seven set-ups were prepared: CD (100 percent), PMS: CD (1:3), PMS:CD (1:2), PMS:CD (1:1), PMS (100 percent), PMS:CD (3:1) and PMS:CD (2:1) and changes in chemical parameters were observed for 60 days. Vermistabilization caused the significant decrease in the level of Cd (32–37 percent), Cr (47.3–80.9 percent), Cu (68.8–88.4 percent), and Pb (95.3–97.5 percent) and substantial increase in EC, total-N, available P and K at the end. At the end, the tissues of inoculated worms showed the high load (mg kg −1 , dry biomass) of Pb (8.81–9.69), Cd (2.31–2.71), Cr (20.7–35.9) and Cu (9.94–11.6), respectively which indicated bioaccumulation of metals by worms. The PMS:CD (2:1 and/or 3:1) appeared to be suitable waste mixture in terms of high metal removal and earthworm growth rates. Bioaccumulation, as quantified using BCF, was in the order: Cd>Cr>Pb>Cu. Results suggested vermiremediation as appropriate technology for bioremediation of heavy metals from PMS. | |
| 11/01/2014 00:00:00 | |
| Link to Article | |
4.5 Bioreactor-based technologies
These approaches use a certain kind of bioreactor for separation.
**Highlights:**
* We proposed a method for sewage water purification of nitrogen and phosphorus compounds on a **disk bioreactor** of full displacement. The developed method of sewage water purification on a bioreactor of full displacement is very promising and we can use it for purification of sewage water, which contains a large amount of organic substances. **The efficiency of purification of mineral nitrogen reaches 98.9 %, phosphates up to 40‒50 %. The total nitrogen content decreases by 4‒6 times and the total phosphorus content ‒ by 2‒2.5 times.** We can use the scheme of purification on troughs and a bioreactor of full displacement for sewage water of dairy industry, livestock farms, communal services, and surface runoff. [ \[Art. #ARTNUM\]](#article-96136-2899297251)
* Compost leachate forms during the composting process of organic material. It is rich in oxidizable organics, ammonia and metals, which pose a risk to the environment if released without proper treatment. An innovative method based on the m**embrane bioreactor (MBR)** technology was developed to treat compost leachate over 39 days. A decrease of more than 99% was achieved for a COD of 116 g/L in the initial leachate. **Ammonia was decreased from 2720 mg/L to 0.046 mg/L**, while the nitrate concentration in the effluent rose to 710 mg/L. The bacteria in the MBR system adjusted to the presence of the leachate, and increased 4 orders of magnitude. **Heavy metals were removed by at least 82.7% except copper.** These successful results demonstrated the membrane bioreactor technology is feasible, efficient method for the treatment of compost leachate.[ \[Art. #ARTNUM\]](#article-96136-2040836780)
| 4.5.1 | Bioreactor-based technologies |
|---|---|
| A novel application of a submerged nanofiltration membrane bioreactor (NF MBR) for wastewater treatment | |
| Nanofiltration (NF) membrane technology has made rapid progress and then extended its application fields. It has obtained in particular the good results in the removal of organic and inorganic matters or microbes in the water and wastewater. To investigate the applicability and characteristics of NF membrane, the membrane bioreactor (MBR) using the cellulose acetate NF membrane was performed to treat synthetic wastewater. A hollow-fiber-type cellulose acetate membrane was chosen to get enough water productivity regardless of its biodegradability. As a result of the experiments, enough water productivity was obtained for 60 days without fatal fouling and membrane cleaning. This raised the applicability of cellulose acetate membrane to the MBR system. Electrolytes were not accumulated in the bioreactor, as its rejection was also low. This enabled the NF MBR to be operated under a low suction pressure and prevented from inhibition against microorganisms, whose activity might be deteriorated by high salt concentration. Nitrification and denitrification happened simultaneously and this might be achieved by the module configuration. The phosphorus was not removed with the loose NF membrane. According to AFM investigation, the cellulose acetate membrane after 71 days has larger voids because of the biodegradation. | |
| 09/01/2002 00:00:00 | |
| Link to Article | |
| 4.5.2 | Bioreactor-based technologies |
| Adaptation and characterization of thermophilic anammox in bioreactors | |
| Abstract Anammox, the oxidation of ammonium with nitrite, is a key microbial process in the nitrogen cycle. Under mesophilic conditions (below 40 °C), it is widely implemented to remove nitrogen from wastewaters lacking organic carbon. Despite evidence of the presence of anammox bacteria in high-temperature environments, reports on the cultivation of thermophilic anammox bacteria are limited to a short-term experiment of 2 weeks. This study showcases the adaptation of a mesophilic inoculum to thermophilic conditions, and its characterization. First, an attached growth technology was chosen to obtain the process. In an anoxic fixed-bed biofilm bioreactor (FBBR), a slow linear temperature increase from 38 to over 48 °C (0.05–0.07 °C d−1) was imposed to the community over 220 days, after which the reactor was operated at 48 °C for over 200 days. Maximum total nitrogen removal rates reached up to 0.62 g N L−1 d−1. Given this promising performance, a suspended growth system was tested. The obtained enrichment culture served as inoculum for membrane bioreactors (MBR) operated at 50 °C, reaching a maximum total nitrogen removal rate of 1.7 g N L−1 d−1 after 35 days. The biomass in the MBR had a maximum specific anammox activity of 1.1 ± 0.1 g NH4+-N g−1 VSS d−1, and the growth rate was estimated at 0.075–0.19 d−1. The thermophilic cultures displayed nitrogen stoichiometry ratios typical for mesophilic anammox: 0.93–1.42 g NO2--Nremoved g−1 NH4+-Nremoved and 0.16–0.35 g NO3--Nproduced g−1 NH4+-Nremoved. Amplicon and Sanger sequencing of the 16S rRNA genes revealed a disappearance of the original “Ca. Brocadia” and “Ca. Jettenia” taxa, yielding Planctomycetes members with only 94–95% similarity to “Ca. Brocadia anammoxidans” and “Ca. B. caroliniensis”, accounting for 45% of the bacterial FBBR community. The long-term operation of thermophilic anammox reactors and snapshot views on the nitrogen stoichiometry, kinetics and microbial community open up the development path of thermophilic partial nitritation/anammox. A first economic assessment highlighted that treatment of sludge reject water from thermophilic anaerobic digestion of sewage sludge may become attractive. | |
| 04/01/2020 00:00:00 | |
| Link to Article | |
| 4.5.3 | Bioreactor-based technologies |
| Aerobic Membrane Bioreactor | |
| Aerobic membrane bioreactors (MBRs) are one of the leading technologies to achieve sustainability in wastewater treatment through reuse, decentralization, and low energy consumption (Fane and Fane 2005; Fawehinmi et al. 2005). In aerobic MBRs, aerated activated sludge is coupled with membrane process to remove dissolved contaminants (carbon and ammonia) and separate solids from the treated municipal or industrial wastewater. Carbon is removed by microorganisms that metabolize the carbon in the presence of dissolved oxygen for microbial growth and respiration (organic carbon reduced to carbon dioxide). Ammonia is removed through ammonia oxidation (nitrification). Nitrification is a microbially mitigated reduction process that occurs in an aquatic environment that contains moderate to high concentrations of ammonia and dissolved oxygen and low concentrations of organic carbon. In submerged MBRs (Fig. 1), microporous (microfiltration (MF) or ultrafiltration (UF) (▶Ultrafiltration)) membranes are immersed in a bioreactor, and water is filtered (▶Permeate) through the membranes using vacuum; suspended solids are retained in the system; and high levels of treatment (including nutrient removal) can be achieved (Judd 2006). The MBR replaces the two-stage conventional activated sludge process (biotreatment and clarification) with a single, integrated process (▶Wastewater Treatment in Membrane Bioreactors). The advantages ofMBRs over conventional treatment have been thoroughly reviewed (Stephenson et al. 2000), and they include product consistency, reduced footprint, reduced sludge production, and nearly complete suspended solid separation from the effluent. Additionally, MBR effluent may be suitable for use as irrigation water, as process water, or as a pretreatment for potable reuse applications (▶Membrane Bioreactors for Reuse; ▶ Potable Water Production) (Lawrence et al. 2002). However, the establishment of membrane bioreactor technology (▶Anaerobic Membrane | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 4.5.4 | Bioreactor-based technologies |
| Highly efficient and low-energy nitrogen removal of sludge reduction liquid by coupling denitrification- partial nitrification-Anammox in an innovative auto-recycling integration device with different partitions | |
| Abstract The denitrification (DN), partial nitrification (PN) and Anammox processes were coupled in an auto-recycling integration device to remove nitrogen from the supernatant of sludge reduction pretreatment. The nitrogen removal performance of the device and the effect of organic matter concentration on the nitrogen transformation were discussed. The results showed that DN, PN and Anammox are well coupled and total nitrogen (TN) removal rate reached 0.85 kg/(m3·d). The pre-DN process can achieve the removal of NO3−-N produced by the back-end PN-Anammox process without the need of reflux pump drive. When the influent NH4+-N concentration was approximately 400 mg/L, the effluent TN concentration was less than 20 mg/L. The fluctuation of organic matter led to changes of nitrogen transformation in the system, and the best ratio of influent CODbio/TN was 0.7–0.9. Nitrosomonas and Candidatus Brocadia played important roles in the nitrogen removal process as the main functional microorganisms of PN and Anammox, respectively. | |
| 04/01/2020 00:00:00 | |
| Link to Article | |
| 4.5.5 | Bioreactor-based technologies |
| Improving the energy balance in wastewater treatment plants by optimization of aeration control and application of new technologies | |
| The methods to improve the energy balance of a wastewater treatment plant (WWTP) by optimization of aeration process control and application of innovative nitrogen removal technologies were overviewed in the study. The control of aeration based on the ABAC (Ammonia-Based Aeration Control) system allows not only for significant savings in electricity consumption, but it can also increase the efficiency of the denitrification process. In addition to obtaining a shortened nitrification path, the use of the AVN (Ammonia vs. Nitrate/Nitrite) system can provide even more efficient nitrogen removal when controlling the process of conventional nitrificationdenitrification. It is expected that the future of the control systems in WWTPs belongs to smart process control systems cooperating with simulation models. The innovative technologies for nitrogen removal are based on the shortcut nitrogen removal pathways. Compared to the conventional nitrification-denitrification, the advantage of the deammonification (partial nitritation/anammox) process is the reduction of both electrical energy demand for aeration and the production of the sludge, as well as no need for the organic carbon source. The significance of pH, temperature, dissolved oxygen concentration, as well as the aeration patterns were emphasized and investigated in details by numerous researchers. The implementation of the innovative nitrogen removal technologies allows to separate organic and nitrogen waste streams and thus maximize energy capture. A study on the implementation of both the chemically enhanced primary treatment and the deammonification process in the sidestream treatment line revealed the potential for an increased biogas production in the anaerobic digester and reduction in the electric energy demand for aeration, while still maintaining the required total nitrogen effluent standard. The proposed upgrades can lead a WWTP from the energy deficit to the energy neutrality. A few WWTPs have already achieved almost 100% (or higher) electricity self-sufficiency using combined approaches and proved the usability of the innovative nitrogen removal technologies. | |
| 01/01/2018 00:00:00 | |
| Link to Article | |
| 4.5.6 | Bioreactor-based technologies |
| Membrane bioreactor technology: A novel approach to the treatment of compost leachate | |
| Abstract Compost leachate forms during the composting process of organic material. It is rich in oxidizable organics, ammonia and metals, which pose a risk to the environment if released without proper treatment. An innovative method based on the membrane bioreactor (MBR) technology was developed to treat compost leachate over 39 days. Water quality parameters, such as pH, dissolved oxygen, ammonia, nitrate, nitrite and chemical oxygen demand (COD) were measured daily. Concentrations of caffeine and metals were measured over the course of the experiment using gas chromatography – mass spectrometry (GC/MS) and inductively coupled plasma – mass spectrometry (ICP–MS) respectively. A decrease of more than 99% was achieved for a COD of 116 g/L in the initial leachate. Ammonia was decreased from 2720 mg/L to 0.046 mg/L, while the nitrate concentration in the effluent rose to 710 mg/L. The bacteria in the MBR system adjusted to the presence of the leachate, and increased 4 orders of magnitude. Heavy metals were removed by at least 82.7% except copper. These successful results demonstrated the membrane bioreactor technology is feasible, efficient method for the treatment of compost leachate. | |
| 11/01/2013 00:00:00 | |
| Link to Article | |
| 4.5.7 | Bioreactor-based technologies |
| Method of agricultural sewage water purification at troughs and a biosorption bioreactor | |
| We proposed a method for sewage water purification of nitrogen and phosphorus compounds on a disk bioreactor of full displacement. The developed method of sewage water purification on a bioreactor of full displacement is very promising and we can use it for purification of sewage water, which contains a large amount of organic substances. The efficiency of purification of mineral nitrogen reaches 98.9 %, phosphates up to 40‒50 %. The total nitrogen content decreases by 4‒6 times and the total phosphorus content ‒ by 2‒2.5 times. We proposed combined purification of surface runoff from agricultural land and household or industrial sewage water on troughs with filtering nozzles and on a bioreactor of full displacement. The conducted microbiological studies showed that the process of purification removes nitrogen compounds complexly: as a result of nitrite-denitrification and of the process of anoxide oxidation. We observed transformation of nitrogen mineral compounds under nitrification on the surface of biodisks in presence of oxygen and inside structural elements of biodisks, which is characteristic of anoxide oxidation during ANAMMOX process. Efficiency of purification of sewage water from the territories for agricultural purposes makes up: for suspended substances ‒ 98 %; for mineral nitrogen ‒ 99 %; for CCO ‒ 99 %; for phosphates ‒ 50 %. We can use the scheme of purification on troughs and a bioreactor of full displacement for sewage water of dairy industry, livestock farms, communal services, and surface runoff. Application of the proposed methods of sewage water purification will contribute to improvement of aquatic ecosystems | |
| 10/11/2018 00:00:00 | |
| Link to Article | |
| 4.5.8 | Bioreactor-based technologies |
| Simultaneous ammonia and Cr (VI) removal by Pseudomonas aeruginosa LX in wastewater | |
| Abstract Inorganic nitrogen and Cr (VI) often co-exist in wastewater and have been a major threat to ecological equilibrium and public health. In this work, we successfully isolated Pseudomonas aeruginosa LX from activated sludge, which was capable of simultaneously degrading ammonia and reducing Cr (VI). Single factor experiments showed that strain LX exhibited efficient ability to remove inorganic nitrogen and it possessed efficient nitrogen removal ability in presence of multiple nitrogen sources. A possible pathway of ammonia removal for strain LX was proposed and was as follows: NH4+-N → NH2OH → NO2--N → NO3--N → NO2--N → NO → N2O → N2. Moreover, more than 80% of 100 mg L-1 NH4+-N could be removed at 30 mg L-1 Cr (VI) and properly increasing ammonia concentration could promote the reduction of Cr (VI). Additionally, immobilized strain LX could degrade ammonia and reduce Cr (VI) to Cr (Ⅲ) well in sequencing batch reactor (SBR). Therefore, strain LX was a suitable candidate to simultaneously remove Cr (VI) and ammonia nitrogen. | |
| 03/03/2020 00:00:00 | |
| Link to Article | |
5. Membrane technologies
BackTechnologies using membranes
5.1 ultrafiltration
Ultrafiltration (UF) is a pressure-driven barrier to suspended solids, bacteria, viruses, endotoxins and other pathogens to produce water with very high purity and low silt density. Ultrafiltration (UF) is a variety of membrane filtration in which hydrostatic pressure forces a liquid against a semi permeable membrane.[\[Source\]](https://crystalquest.com/pages/what-is-ultrafiltration#:\~:text=Ultrafiltration%20(UF)%20is%20a%20pressure,against%20a%20semi%20permeable%20membrane.)
**Highlights:**
* Micellar-enhanced ultrafiltration(MEUF) is a powerful treatment process developed recently to remove heavy metals from wastewater,which combines ultrafiltration with surfactant technology. Competitive adsorption of Cd2+,Zn2+,Pb2+ to SDS micelle micellar-enhanced ultrafiltration(MEUF) was studied for single solute and mixed solute containing cadmium ions,zinc ions and plumbum ions with sodium dodecyl sulfate(SDS) as surfactant. Results show that with the wastewater containing a variety of bivalence heavy metal ions, competitive adsorption to SDS micelle exists among various ions, and the sequence of competitive adsorption is Pb2+Zn2+Cd2+. [\[Art. #ARTNUM\]](#article-96074-2353167906)
* Based on this concept, we developed an integrated process taking advantage of the **strong adsorption abilities of in-situ Al or Fe hydrolytic flocs and excellent separation properties of ultrafiltration (UF) membranes.** **By controlling the aeration rate, injection frequency and the solution pH, membrane fouling was alleviated, especially under weakly acidic conditions. Additionally, owing to the higher rejection efficiency of the UF membrane, the effluent quality was improved, including the iron concentration, turbidity, and chromaticity.** This innovative separation method shows promising potential for application in removing heavy metals in water treatment.[ \[Art. #ARTNUM\]](#article-96074-2611225203)
* In this work, a novel positively charged tight ultrafiltration (PCTUF) membrane was developed to remove heavy metal cations (Mn 2+ , Co 2+ , Ni 2+ , Zn 2+ and Cd 2+ ) from contaminated waters via electrostatic repulsion mechanism. The results revealed that the prepared PCTUF membrane with its high perm-selectivity performance provides a worthy reference for highly efficient removal of heavy metal cations. [\[Art. #ARTNUM\]](#article-96074-2922823182)
| 5.1.1 | ultrafiltration |
|---|---|
| A positively charged tight UF membrane and its properties for removing trace metal cations via electrostatic repulsion mechanism | |
| Abstract The development of highly efficient membranes technology using low-pressure driven filtration process, is one of the principal challenges in the wastewater treatment field, especially those aimed at the removal of trace heavy metals. In this work, a novel positively charged tight ultrafiltration (PCTUF) membrane was developed to remove heavy metal cations (Mn 2+ , Co 2+ , Ni 2+ , Zn 2+ and Cd 2+ ) from contaminated waters via electrostatic repulsion mechanism. The PCTUF membrane was fabricated from a new polymer with poly (vinyl chloride co dimethylaminoethyl methacrylate), P (VC- co -DMA) via a nonsolvent induce phase separation (NIPS) process and following facile surface quaternization. The quaternization conditions, the pore structures and chemical properties of the membranes were investigated in detail. The optimally quaternized membrane possessed a positively charged surface and 3.27 nm charged channel with the water permeability of 84 L m −2 h −1 bar −1 . The rejections of heavy metal cations surpassed 95% for feed solutions containing 10 ppm heavy metal. Moreover, the influences of feed concentrations and the operating condition with pressure and pH on the membrane performances were also investigated. The results revealed that the prepared PCTUF membrane with its high perm-selectivity performance provides a worthy reference for highly efficient removal of heavy metal cations. | |
| 03/01/2019 00:00:00 | |
| Link to Article | |
| 5.1.2 | ultrafiltration |
| Adsorption of surfactant micelles and Cd2+/Zn2+ in micellar-enhanced ultrafiltration | |
| Abstract Micellar-enhanced ultrafiltration (MEUF) is a powerful treatment developed to remove heavy metals from wastewater. Efficient removal of Cd 2+ /Zn 2+ from wastewater was performed by MEUF using a polysulfone hollow ultrafiltration membrane, with sodium dodecyl sulfate (SDS) as the surfactant. The adsorption of surfactant micelles and Cd 2+ /Zn 2+ in MEUF was studied by changing the surfactant dosage and the Cd 2+ /Zn 2+ concentration in the feed. In addition, kinetics, adsorption isotherms, and thermodynamic rules were analyzed, and X-ray photoelectron spectroscopy (XPS) was conducted. It was found that when the Cd 2+ /Zn 2+ feed concentration was 50 mg/L, and the SDS dosage reached 2.15 g/L, the concentration of heavy metal ions in the permeate stabilized at around 1–4 mg/L, and the adsorption of Cd 2+ /Zn 2+ on SDS micelles followed second-order kinetics and the Langmuir isotherm laws. Adsorption is a spontaneous endothermic process in which the adsorption force is principally the attraction of opposite electrical charges. | |
| 11/01/2010 00:00:00 | |
| Link to Article | |
| 5.1.3 | ultrafiltration |
| Ammonia removal from chicken manure digestate through vapor pressure membrane contactor (VPMC) and phytoremediation | |
| Abstract Ammonia removal from synthetic ammonia solutions and chicken manure digestate via vapor pressure membrane contactor through Polytetrafluoroethylene (PTFE) membrane was investigated. The highest ammonia mass flux, separation factor, and removal efficiencies of 28.6 ± 0.2 g N/m 2 h, 53.9 ± 10.7, and 97.6 ± 0.7% were observed for synthetic solutions, respectively. Ammonia removal efficiency of 93.6 ± 1.9% through membrane contactor was observed for chicken manure digestate decreasing the total ammonia concentration from 3643.5 ± 67.2 to 230.9 ± 46.2 mg N/L. Phytoremediation via Lemna minor species was used as a polishing step to remove remaining ammonia from the membrane contactor effluent. Total ammonia concentration was then decreased below 2 mg N/L through evaporation, nitrification, and plant uptake processes occurring in the phytoremediation containers. This study reveals that ammonia can be successfully removed via VPMC and phytoremediation systems and the process is implementable as it can be coupled to anaerobic digestion processes to recover ammonia and to prevent ammonia inhibition. | |
| 02/01/2019 00:00:00 | |
| Link to Article | |
| 5.1.4 | ultrafiltration |
| Biosorption of Heavy Metal by Algae Biomass in Surface Water | |
| Discharging wastewater containing heavy metals of Cu, Pb, Zn and Cd into water bodies can cause toxicity in plants and aquatic animals and some of them will be unable to survive except algae. Wastewater treatment method to remove heavy metal contaminants includes chemical precipitation, ion exchange, membrane, filtration, adsorption using activated carbon. However, these methods are either expensive or have other disadvantages such as high energy consumption and inefficiencies when existing heavy metals are at trace concentration. Biosorption using algae biomass can be an alternative method to eliminate heavy metals. The objective of the project is to investigate the capability of Marine Algae (MA) and Freshwater Algae (FA) bi-omass in adsorbing heavy metals of Cu, Pb, Zn and Cd from water medium using synthetic water and industrial water. MA and FA were obtained from the eastern coast of Pulau Ubin and local fish farm respectively. After being fully washed with deionised water, dried in a furnace for 105°C, they are grinded to pass 1 mm2 of siever. MA and FA were characterised using FTIR to determine their functional groups. An industrial water was collected from industrial discharge from metal fac-tories in northern side of Singapore. Effect of adsorption time, adsorbent concentra-tion, and pH were studied. The result showed that FA and MA had a higher capability in adsorbing a total metal of about 40 ppm level from an industrial water, or 4 times than synthetic water concentration, at the same adsorbent dosage of 50 mg. In con-clusion, the presence of various functional groups, hydroxyl, carboxylic and amine groups, in all MA and FA samples had enabled the algae biomass to adsorb heavy metals of Cu, Pb, Cd and Zn from synthetic and industrial water. Due to their bio-sorptive properties and fast adsorption capability, algae could be a potential method for cleaning up surface water or post-treatment of wastewater and minimise the cost of eutrophication. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 5.1.5 | ultrafiltration |
| Competitive adsorption of Cd~(2+),Zn~(2+),Pb~(2+) to SDS micelle in micellar-enhanced ultrafiltration | |
| Micellar-enhanced ultrafiltration(MEUF) is a powerful treatment process developed recently to remove heavy metals from wastewater,which combines ultrafiltration with surfactant technology.Competitive adsorption of Cd2+,Zn2+,Pb2+ to SDS micelle micellar-enhanced ultrafiltration(MEUF) was studied for single solute and mixed solute containing cadmium ions,zinc ions and plumbum ions with sodium dodecyl sulfate(SDS) as surfactant.Results show that with the wastewater containing a variety of bivalence heavy metal ions,competitive adsorption to SDS micelle exists among various ions,and the sequence of competitive adsorption is Pb2+Zn2+Cd2+. The experiment has clarified the cooperative adsorption relation of Cd-Zn and the resistant adsorption relation of Zn-Pb. | |
| 01/01/2008 00:00:00 | |
| Link to Article | |
| 5.1.6 | ultrafiltration |
| Enhanced ammonia recovery from wastewater by Nafion membrane with highly porous honeycomb nanostructure and its mechanism in membrane distillation | |
| Abstract Removing nitrogen from wastewater by conventional treatment methods requires substantial energy, only to release it back to the atmosphere as gaseous nitrogen. Herein, we investigated the applicability of membrane distillation (MD) in resource recovery from sludge digestate by controlling the volatility and pressure of the vapor transport across the membrane to concentrate ammonia in the permeate stream. A mixture of Nafion ionomer and Multiwall Carbon Nanotubes (MWCNTs) were incorporated into a Poly (vinylidene fluoride-co-hexafluoropropene; PVDF-HFP) nanofiber matrix to fabricate a nanoporous honeycomb Nafion membrane featuring high recovery and increased mechanical strength. Theoretical modeling was conducted to predict the expected performance of the fabricated Nafion membrane under different operation conditions and to reveal the mechanism behind the enhanced recovery of Nafion membranes in the MD process. The resultant Nafion (8%)/MWCNT (2.5%)/PVDF-HFP nanofibrous membrane showed up to three times higher ammonia recovery compared to the commercial PVDF membrane from a feed with an ammonia concentration of 300 mg/L. The theoretical analysis quantitatively revealed that the Nafion containing membrane can not only suppress the negative effect of membrane's structural resistance on the ammonia recovery efficiency but also enhance the efficiency. In addition, we also uncovered that the effect of Nafion on ammonia recovery efficiency was maximized when the Nafion 8% membrane was employed. This study demonstrated an innovative and realistically applicable MD treatment process for recovering resource, which integrates low-grade heat and has scaling-up potential for wastewater treatment plants. | |
| 07/01/2019 00:00:00 | |
| Link to Article | |
| 5.1.7 | ultrafiltration |
| Synergistic process using Fe hydrolytic flocs and ultrafiltration membrane for enhanced antimony(V) removal | |
| Abstract Antimony (Sb) is harmful to human health, and Sb(V) is much more difficult to remove from water than other toxic elements such as arsenic (As). Theoretical studies have suggested that in situ flocs have stronger adsorption ability toward heavy metals than pre-made adsorbents. We believe that rational design of in situ flocs and the associated device structure will enable a floc-based device to be utilized in the removal of heavy metals. Based on this concept, we developed an integrated process taking advantage of the strong adsorption abilities of in-situ Al or Fe hydrolytic flocs and excellent separation properties of ultrafiltration (UF) membranes. We found that flocs could be well dispersed in a membrane tank with aeration from the bottom, and Fe-based flocs performed better in removing Sb(V) and alleviating membrane fouling than Al-based flocs. We also demonstrated that higher Sb(V) removal efficiency was induced with continuous injection, and lower solution pH. By controlling the aeration rate, injection frequency and the solution pH, membrane fouling was alleviated, especially under weakly acidic conditions. Additionally, owing to the higher rejection efficiency of the UF membrane, the effluent quality was improved, including the iron concentration, turbidity, and chromaticity. This innovative separation method shows promising potential for application in removing heavy metals in water treatment. | |
| 09/01/2017 00:00:00 | |
| Link to Article | |
| 5.1.8 | ultrafiltration |
| The Nanomembrane Toilet: Membranes for water recovery in decentralised sanitation systems | |
| Poster presented at the Cranfield Doctoral Network Annual Event 2018.In this research, the Nanomembrane Toilet is introduced as a single household sanitation system independent of grid produced power. To address paucity of information on super-concentrated wastewater characterisation, chemical oxygen demand (COD), ammoniacal nitrogen, and E.Coli bacteria are analysed in the wastewater storage tank. A small-scale combustor is developed (Onabanjo et al., 2016) to operate on the faecal sludge phase, producing low-grade heat that is used to provide the vapour pressure gradient for thermally-driven membrane separation of water from faecally contaminated urine (FCU). Subsequently, a membrane technology is developed that can provide a single-stage treatment process, separating clean water from FCU. In this study, the impact of temperature on water recovery from FCU (urine:faece 56:1) by membranes (PTFE, nominal pore size 0.1 µm) is investigated. Out of 40, 50, and 60 ⁰C operational temperature values, operation at 60 c is shown to enable the process for the removal of organics, inorganics, and pathogens, sufficient to meet the ISO/PC 305 standard for sustainable non-sewered sanitation systems (American National Standards Institute, 2016). Furthermore, influence of faecal concentration in the FCU (at optimised temperature of 60 ⁰C) on the produced water quality is studied. The results show that high faecal concentration leads to high ammonium formation in the feed, hence faster ammonia breakthrough is observed. Lastly, the membrane pore size was optimised for the treatment of FCU at constant faecal concentration and temperature. It is concluded that only 0.1 µm membrane pore size is capable of removing ammonia, COD, and E.Coli to the proposed ISO standard at both 40 and 60 ⁰C. Importantly, this study has demonstrated that through integration of this modularised componentry into the Nanomembrane Toilet, single household sanitation can be delivered, independent of external power sources and infrastructure. | |
| 10/22/2018 00:00:00 | |
| Link to Article | |
5.2 nanofiltration (NF)
Nanofiltration is a membrane filtration-based method that uses nanometer sized through-pores that pass through the membrane. Nanofiltration membranes have pore sizes from 1-10 nanometers, smaller than that used in microfiltration and ultrafiltration, but just larger than that in reverse osmosis.[\[Wiki\]](https://en.wikipedia.org/wiki/Nanofiltration#:\~:text=Nanofiltration%20is%20a%20membrane%20filtration,than%20that%20in%20reverse%20osmosis.)
**Highlights:**
* One must separate phosphorus from the heavy metals in order to produce fertilizers of high quality. Among various available methods, nanofiltration (NF) has been demonstrated to be a feasible and promising option when the sewage sludge undergoes acidic dissolution and the operating pH is around 2. Because the performance of commercially available thin film composite (TFC) NF membranes reported thus far has great room for improvement, the development of highly permeable positively charged NF membranes is recommended. To this aim, a NF membrane that is desirable for phosphorus recovery was fabricated via interfacial polymerization of polyethylenimine (PEI) and trimesoyl chloride (TMC) on a porous poly(ether sulfone) (PES) membrane substrate.[ \[Art. #ARTNUM\]](#article-96121-2510602979)
* This is a report of the first attempt to develop a composite NF membrane comprising a molecularly designed pentablock copolymer selective layer for the removal of heavy metal ions. The resultant NF membrane has a mean effective pore diameter of 0.50 nm, a molecular weight cutoff of 255 Da, and a reasonably high pure water permeability (A) of 2.4 LMH/bar. The newly developed NF membrane can effectively remove heavy metal cations such as Pb2+, Cd2+, Zn2+, and Ni2+ with a rejection of >98.0%.[ \[Art. #ARTNUM\]](#article-96121-2314982393)
* In order to effectively separate chloride (such as NaCl) and sulfate (such as Na 2 SO 4 ) for high saline wastewater recycling, one commercial NF membrane (named Desal-DL) was employed in the permeation of the single and binary salt solutions of NaCl and Na 2 SO 4 with a lab-scale cross-flow batch module, where the salt concentration ranged from 4 to 96 g L −1 and the operating pressures varied from 0.6 to 2.4 MPa as well as the temperature was kept under room temperature. The experimental results showed that the Desal-DL NF membrane had a low rejection to NaCl and a high rejection to Na 2 SO 4 for single salt solutions. [\[Art. #ARTNUM\]](#article-96121-2324824251)
* For the first time, thin film nanocomposite (TFN) nanofiltration membranes incorporated with graphene oxide (GO) were synthesized and used to separate phosphorus from water source of different properties. [\[Art. #ARTNUM\]](#article-96121-2767186783)
| 5.2.1 | nanofiltration (NF) |
|---|---|
| Molecular Design of Nanofiltration Membranes for the Recovery of Phosphorus from Sewage Sludge | |
| With the rapid depletion of mineral phosphorus, the recovery of phosphorus from sewage sludge becomes increasingly important. However, the presence of various contaminants such as heavy metals in sewage sludge complicates the issue. One must separate phosphorus from the heavy metals in order to produce fertilizers of high quality. Among various available methods, nanofiltration (NF) has been demonstrated to be a feasible and promising option when the sewage sludge undergoes acidic dissolution and the operating pH is around 2. Because the performance of commercially available thin film composite (TFC) NF membranes reported thus far has great room for improvement, the development of highly permeable positively charged NF membranes is recommended. To this aim, a NF membrane that is desirable for phosphorus recovery was fabricated via interfacial polymerization of polyethylenimine (PEI) and trimesoyl chloride (TMC) on a porous poly(ether sulfone) (PES) membrane substrate. Through an optimization of the interf... | |
| 10/03/2016 00:00:00 | |
| Link to Article | |
| 5.2.2 | nanofiltration (NF) |
| Novel Nanofiltration Membranes Consisting of a Sulfonated Pentablock Copolymer Rejection Layer for Heavy Metal Removal | |
| Facing stringent regulations on wastewater discharge containing heavy metal ions, various industries are demanding more efficient and effective treatment methods. Among the methods available, nanofiltration (NF) is a feasible and promising option. However, the development of new membrane materials is constantly required for the advancement of this technology. This is a report of the first attempt to develop a composite NF membrane comprising a molecularly designed pentablock copolymer selective layer for the removal of heavy metal ions. The resultant NF membrane has a mean effective pore diameter of 0.50 nm, a molecular weight cutoff of 255 Da, and a reasonably high pure water permeability (A) of 2.4 LMH/bar. The newly developed NF membrane can effectively remove heavy metal cations such as Pb2+, Cd2+, Zn2+, and Ni2+ with a rejection of >98.0%. On the other hand, the membrane also shows reasonably high rejections toward anions such as HAsO42– (99.9%) and HCrO4– (92.3%). This performance can be attributed ... | |
| 12/02/2014 00:00:00 | |
| Link to Article | |
| 5.2.3 | nanofiltration (NF) |
| Phosphorus recovery from sewage sludge with a hybrid process of low pressure wet oxidation and nanofiltration | |
| Abstract Phosphorus recovery from sewage sludge will become increasingly important within the next decades due to depletion of mineral phosphorus resources. In this work a new process concept was investigated, which aims at realising phosphorus recovery in a synergistic way with the overall sewage sludge treatment scheme. This process combines a low pressure wet oxidation for sewage sludge decomposition as well as phosphorus dissolution and a nanofiltration process to separate phosphorus from heavy metals and obtain a clean diluted phosphoric acid, from which phosphorus can be recovered as clean fertiliser. It was shown that this process concept is feasible for sewage sludge for wastewater treatment plants that apply enhanced biological removal or precipitation with alumina salts for phosphorus removal. The critical parameter for phosphorus dissolution in the low pressure wet oxidation process is the iron concentration, while in the nanofiltration multi-valent cations play a predominant role. In total, a phosphorus recovery of 54% was obtained for an exemplary wastewater treatment plant. Costs of the entire process are in the same range as conventional sewage sludge disposal, with the benefit being phosphorus recovery and reduced emission of greenhouse gases due to avoidance of sludge incineration. | |
| 04/01/2012 00:00:00 | |
| Link to Article | |
| 5.2.4 | nanofiltration (NF) |
| Removal of Heavy Metals from Electroplating Wastewater by Thin-Film Composite Nanofiltration Hollow-Fiber Membranes | |
| In this study, thin-film composite nanofiltration (NF) hollow-fiber membranes were used to remove heavy metals from actual electroplating wastewater. The effects of the operating pressure, feed temperature, and feed pH on the membrane performance for the treatment of electroplating wastewater were investigated. The rejection rates for chromium, copper, and nickel ions reached 95.76%, 95.33%, and 94.99%, respectively, at 0.4 MPa. With a rise in the feed temperature, the permeate flux increased while the rejection rates of heavy metals did not significantly change. It was evident that the feed pH greatly affected the permeate flux and heavy-metal rejection as well. In addition, all of the rejection rates of heavy metals by the membrane were over 94.8% throughout the electroplating wastewater concentration process. Also, the NF hollow-fiber membrane showed good stability in electroplating wastewater with a pH value of 2.31. | |
| 12/11/2013 00:00:00 | |
| Link to Article | |
| 5.2.5 | nanofiltration (NF) |
| Selective separation of chloride and sulfate by nanofiltration for high saline wastewater recycling | |
| Abstract In order to effectively separate chloride (such as NaCl) and sulfate (such as Na 2 SO 4 ) for high saline wastewater recycling, one commercial NF membrane (named Desal-DL) was employed in the permeation of the single and binary salt solutions of NaCl and Na 2 SO 4 with a lab-scale cross-flow batch module, where the salt concentration ranged from 4 to 96 g L −1 and the operating pressures varied from 0.6 to 2.4 MPa as well as the temperature was kept under room temperature. The experimental results showed that the Desal-DL NF membrane had a low rejection to NaCl and a high rejection to Na 2 SO 4 for single salt solutions. While for binary salt solutions, the membrane presented a bit higher rejection to SO 4 2− and much lower rejection to Cl − , even special negative rejection to Cl − was observed when the concentration of Na 2 SO 4 was high. This implies that NF is suitable to be used for the separation of Na 2 SO 4 and NaCl from their binary solution, where Na 2 SO 4 could be retained by the NF membrane and concentrated to high concentration while NaCl could pass through the membrane and might be diluted to low concentration with a diafiltration operation mode. Finally the selective separation of Na 2 SO 4 and NaCl by NF diafiltration was simulated for the binary salt solution containing 23.4 g L −1 NaCl and 8.76 g L −1 Na 2 SO 4 . A highly concentrated solution of Na 2 SO 4 (71.74 g L −1 ) and a relatively pure solution of NaCl (20.79 g L −1 ) were obtained, which favored the post-treatment of high saline wastewater for inorganic salts recycling. | |
| 06/01/2016 00:00:00 | |
| Link to Article | |
| 5.2.6 | nanofiltration (NF) |
| Thin-Film Nanocomposite Nanofiltration Membranes Incorporated with Graphene Oxide for Phosphorus Removal | |
| For the first time, thin film nanocomposite (TFN) nanofiltration membranes incorporated with graphene oxide (GO) were synthesized and used to separate phosphorus from water source of different properties. Prior to phosphorus removal tests, the properties of the two TFN membranes (TFN-1 and TFN-2 with GO loadings of 0.15 and 0.3 wt%, respectively) and one control thin film composite (TFC) membrane were subject to standard characterizations to determine pure water flux, salt rejection, surface hydrophilicity, pore size and porosity. Results showed that upon incorporation of GO, the water flux of composite membrane could be significantly improved with minimum decrease in salt rejection. This is mainly due to improved surface hydrophilicity coupled with enlarged pore size and overall structural porosity. The TFN-1 membrane in particular is found to perform better owing to its good combination of water flux and solute rejection. When tested with feed solution containing 10 mg L-1 phosphorus, the TFN-1 membrane showed water flux of 13.2 L m-2 h-1, i.e., 17.9% higher than the water flux achieved by the TFC membrane. Its total phosphorus rejection meanwhile recorded at 80% compared to 84% achieved by the TFC membrane. The TFN-1 membrane also exhibited higher water flux and comparable phosphorus rejection in comparison to the TFC membrane when both membranes were used to treat phosphorus solution containing humic acids. Although the incorporation of GO tended to produce the TFN membrane with larger surface pore size, the significant improvement in membrane water flux and surface hydrophilicity had outweighed the small decrease in phosphorus removal rate. | |
| 02/01/2018 00:00:00 | |
| Link to Article | |
5.3 Reverse osmosis
Formally, reverse osmosis is the process of forcing a solvent from a region of high solute concentration through a semipermeable membrane to a region of low-solute concentration by applying a pressure in excess of the osmotic pressure.[\[Wiki\]](https://en.wikipedia.org/wiki/Reverse_osmosis#:\~:text=Formally%2C%20reverse%20osmosis%20is%20the,excess%20of%20the%20osmotic%20pressure.)
**Highlights:**
* In this study, low-pressure reverse osmosis was analyzed to remove heavy metal ions (nickel and copper) from highly diluted feed flows. Given the ability of these ions to form complexes with EDTA, the effectiveness of a preliminary stage of complexation was also evaluated. The experimental system consisted of a reactor with commercial flat membrane of polyamide and cross flow. Studies employing solutions of single ions and also mixture of ions in different concentration ranges reached removals of 99%. [ \[Art. #ARTNUM\]](#article-96290-2311502662)
* The results showed that high removal efficiency of the heavy metals could be achieved by RO process (98% and 99% for copper and cadmium, respectively). [\[Paper\]](https://www.sciencedirect.com/science/article/pii/S1878535210001334#s0055)
* R.O is a membrane filtration process where water can easily pass through a membrane however cationic compounds are retained. The pore size of the R.O membrane is 0.1nm. R.O can be used for all solutions which have less quantity of metal dissolved in the millimolar or micromolar range. [\[Paper\]](https://www.researchgate.net/publication/331952883_Remediation_of_Nickel_ion_from_wastewater_by_applying_various_techniques_a_review)
| 5.3.1 | Reverse osmosis |
|---|---|
| Application of reverse osmosis process associated with EDTA complexation for nickel and copper removal from wastewater | |
| AbstractIn this study, low-pressure reverse osmosis was analyzed to remove heavy metal ions (nickel and copper) from highly diluted feed flows. Given the ability of these ions to form complexes with EDTA, the effectiveness of a preliminary stage of complexation was also evaluated. The experimental system consisted of a reactor with commercial flat membrane of polyamide and cross flow. Studies employing solutions of single ions and also mixture of ions in different concentration ranges reached removals of 99%. The complexing agent forms a larger complex than the single ion in aqueous phase, thus increasing ion removal in terms of final concentration in permeate. Experiments made at different pressures showed the increase in pressure has an effect on increasing rejection and permeate flow, but the applied pressure of 0.5 MPa is sufficient to achieve 98.5% removal of metal ions and a flow of about 13 L/h m2. | |
| 09/01/2016 00:00:00 | |
| Link to Article | |
5.4 Electrodialysis
Electrodialysis is used to transport salt ions from one solution through ion-exchange membranes to another solution under the influence of an applied electric potential difference. This is done in a configuration called an electrodialysis cell. [\[Wiki\]](https://en.wikipedia.org/wiki/Electrodialysis)
**Highlights:**
* The raffinate generated during copper ore hydrometallurgical processing is difficult to be treated because it is strongly acidic, and has high concentrations of heavy metals (Iron, Zinc, Copper etc). **In this study, a bipolar membrane electrodialysis (BMED) system was studied for treatment of this challenging stream because in which salts can be converted into their corresponding acids and bases, which enables resource recovery in raffinate.** The target was to reuse the raffinate as a leaching influent, to achieve zero discharge of wastewater. It was found that 85.9% of SO42- in the raffinate could be recovered by the formation of H2SO4. The removal rates of heavy metals were 99.3% (iron), 99.1% (zinc), 99.0% (copper), 84.9% (nickel), 70.6% (chromium), 95.8% (cadmium), and 94.8% (arsenic). The heavy metal cations were mainly removed in the heavy metals chamber (HMC) and anions were mainly removed in the acid compartment. It was concluded that the raffinate can be used as a leaching solution after treatment and the studied BMED process is an effective technique for the treatment of raffinate.[ \[Art. #ARTNUM\]](#article-96117-2977176722)
* Electro-dialysis is separation method where ions are shifted over ion exchange resin with the help of electricity between two electrodes. Tzanetakis et al. investigate the removal of Cobalt and Nickel from their sulphate solution by using two cation exchange and an anion exchange membrane, a stainless steel cathode and platinum oxide based coated titanium cobalt, a suitable complexing agent is EDTA. [\[Paper\]](https://www.researchgate.net/publication/331952883_Remediation_of_Nickel_ion_from_wastewater_by_applying_various_techniques_a_review)
| 5.4.1 | Electrodialysis |
|---|---|
| Phosphorus recovery from sewage sludge ash with bioleaching and electrodialysis | |
| Abstract Phosphorus is an essential element for all living organisms and for plants. However, phosphate rock, which is the main source of phosphorus, is limited and thus it must be recovered from secondary sources like sewage sludge ash (SSA). SSA is one of the most promising secondary sources because it contains considerable amounts of phosphorus. The drawback of SSA as a secondary source is the presence of heavy metals along with phosphorus. In this study, a bioleaching process was applied to solubilize the phosphorus more economically, thus bioleaching bacteria was used to obtain acidic conditions for phosphorus leaching. For this purpose, batch bioleaching experiments were carried out with Sulfur oxidizing bacteria (SOB) to optimize the process in terms of phosphorus dissolution. Experiments were conducted with different amounts of ash, inoculum volumes, and sulfur concentrations. Because the application of the bioleaching process leads to solubilization of heavy metals beside phosphorus, an electrodialysis process was used to separate phosphorus from heavy metals. Electrodialysis experiments were performed in a 3 compartment electrodialysis reactor with gold coated copper electrodes. The maximum phosphorus bioleaching was obtained with 2 g of ash, 40% inoculum, and 10 g.l-1 elemental sulfur. Electrodialysis studies with gold coated copper electrodes lasted for 14 days and 24.6% of the phosphorus was transported to the anode. | |
| 10/01/2019 00:00:00 | |
| Link to Article | |
| 5.4.2 | Electrodialysis |
| Treatment of raffinate generated via copper ore hydrometallurgical processing using a bipolar membrane electrodialysis system | |
| Abstract The raffinate generated during copper ore hydrometallurgical processing is difficult to be treated because it is strongly acidic, and has high concentrations of heavy metals (Iron, Zinc, Copper etc). In this study, a bipolar membrane electrodialysis (BMED) system was studied for treatment of this challenging stream because in which salts can be converted into their corresponding acids and bases, which enables resource recovery in raffinate. The target was to reuse the raffinate as a leaching influent, to achieve zero discharge of wastewater. It was found that 85.9% of SO42- in the raffinate could be recovered by the formation of H2SO4. The removal rates of heavy metals were 99.3% (iron), 99.1% (zinc), 99.0% (copper), 84.9% (nickel), 70.6% (chromium), 95.8% (cadmium), and 94.8% (arsenic). The heavy metal cations were mainly removed in the heavy metals chamber (HMC) and anions were mainly removed in the acid compartment. A current density of 3.0 mA/cm2, a volume ratio between the raffinate chamber (RC) and the HMC 1:15, and a duration of 40 h were the optimal experimental parameters. Increasing the RC number from one to two and three increased the current efficiency from 54.0% to 106.9% (two) and 157.9% (three), and decreased the specific energy consumption from 0.160 to 0.108 and 0.089 kWh/L of raffinate. It was concluded that the raffinate can be used as a leaching solution after treatment and the studied BMED process is an effective technique for the treatment of raffinate. | |
| 09/01/2019 00:00:00 | |
| Link to Article | |
5.5 Electrically conducting membranes
New concepts of separation based on electrochemical interactions were realized due to the successful developments of the electrically conductive membrane (called electromembrane). This electromembrane differs from the conventional ion exchange membrane due to the nature of the separation mechanism. The separation in an electromembrane is based on the electrical potential and/or magnetic field “barrier” generated by passing current through the membrane, while the separation in a conventional ion-exchange membrane relies on the relative ionic affinity of the compounds being separated. It is this characteristic which provides a unique opportunity for this new class of membrane.[\[Paper\]](https://www.sciencedirect.com/science/article/abs/pii/S0376738800808844)
**Highlights:**
* The goal of this dissertation is to demonstrate fouling prevention and foulant removal on carbon nanotube-modified (CNT) electrically conductive UF, NF and RO membranes. First, mineral scaling was prevented and removed by applying an external anodic electrical potential to an electrically conducting CNT – polyamide RO membrane. The results demonstrate that CaCO3 scaling was efficiently removed by the intermittent application of 2.5V and CaSO4 scaling can be prevented by the continuous application of 1.5V with the membrane as the anode. Second, biofouling and organic fouling were prevented while treating anaerobic sequencing batch reactor effluent by using electrically conducting UF and NF membranes. The modified membrane can be used to degrade organic compounds and perform in situ oxidative cleaning of the fouled membrane without any additional oxidizing chemical reagents[ \[Art. #ARTNUM\]](#article-96155-2898647488)
* In the present study, the electromembrane extraction (EME) procedure was used for extraction of heavy metal cations from aqueous samples. The obtained results showed that more than 71.2% of the free ions were extracted from primeval aqueous samples. Moreover, the results indicated that this technique can be used in large-scale extraction of heavy metal cations from aqueous solutions.[\[Paper\]](https://pubs.rsc.org/en/content/articlelanding/2015/ay/c5ay00243e#!divAbstract)
| 5.5.1 | Electrically conducting membranes |
|---|---|
| A positively charged tight UF membrane and its properties for removing trace metal cations via electrostatic repulsion mechanism | |
| Abstract The development of highly efficient membranes technology using low-pressure driven filtration process, is one of the principal challenges in the wastewater treatment field, especially those aimed at the removal of trace heavy metals. In this work, a novel positively charged tight ultrafiltration (PCTUF) membrane was developed to remove heavy metal cations (Mn 2+ , Co 2+ , Ni 2+ , Zn 2+ and Cd 2+ ) from contaminated waters via electrostatic repulsion mechanism. The PCTUF membrane was fabricated from a new polymer with poly (vinyl chloride co dimethylaminoethyl methacrylate), P (VC- co -DMA) via a nonsolvent induce phase separation (NIPS) process and following facile surface quaternization. The quaternization conditions, the pore structures and chemical properties of the membranes were investigated in detail. The optimally quaternized membrane possessed a positively charged surface and 3.27 nm charged channel with the water permeability of 84 L m −2 h −1 bar −1 . The rejections of heavy metal cations surpassed 95% for feed solutions containing 10 ppm heavy metal. Moreover, the influences of feed concentrations and the operating condition with pressure and pH on the membrane performances were also investigated. The results revealed that the prepared PCTUF membrane with its high perm-selectivity performance provides a worthy reference for highly efficient removal of heavy metal cations. | |
| 03/01/2019 00:00:00 | |
| Link to Article | |
| 5.5.2 | Electrically conducting membranes |
| Membrane Performance Enhancement Using Electrically Conducting Membranes | |
| Author(s): Duan, Wenyan | Advisor(s): Jassby, David | Abstract: Water shortage is a pervasive problem which has plagued societies for centuries. Recently, membrane technology has offered an effective and robust water treatment method for water sustainability due to great improvements in membrane performance. Depending on the intended applications, microfiltration (MF), ultrafiltration (UF), nano-filtration (NF) or reverse osmosis (RO) membranes can be used individually or in combination to achieve a specific water quality goal. However, a major challenge facing these technologies is membrane fouling, where particulates in the feed stream are deposited or developed on the membrane surface during the filtration process. Membrane fouling results in performance deterioration, lifetime shortening, and ultimately, increased operational costs. Therefore, membrane cleaning and fouling control or prevention are critical research topics for membrane development. The goal of this dissertation is to demonstrate fouling prevention and foulant removal on carbon nanotube-modified (CNT) electrically conductive UF, NF and RO membranes. First, mineral scaling was prevented and removed by applying an external anodic electrical potential to an electrically conducting CNT – polyamide RO membrane. The results demonstrate that CaCO3 scaling was efficiently removed by the intermittent application of 2.5V and CaSO4 scaling can be prevented by the continuous application of 1.5V with the membrane as the anode. Second, biofouling and organic fouling were prevented while treating anaerobic sequencing batch reactor effluent by using electrically conducting UF and NF membranes. The continuous application of negative 5V to the UF membrane surface prevents organic fouling and allows good membrane performance while treating complex wastewater streams for long periods of time. The application of positive potentials to the NF membranes has also been shown to increase fouling and hinder cleaning and recovery. Third, a highly conductive and anodically stable polyaniline coated UF membrane was designed and used as a flow through electrode. Results show that the polyaniline coated CNT membrane had a significantly reduced degradation rate under high anodic potentials in a pH controlled environment when compared with polyvinyl alcohol crosslinked CNT membrane. The modified membrane can be used to degrade organic compounds and perform in situ oxidative cleaning of the fouled membrane without any additional oxidizing chemical reagents. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
5.6 Membrane adsorption
A membrane adsorbent is made by connecting functional groups to the surface and pore wall of polymer membranes; the target pollutants are selectively adsorbed to the functional group. The membrane adsorbent effectively combines the filtration performance of the membrane.[\[Paper\]](https://link.springer.com/article/10.1007/s13201-018-0661-6#:\~:text=A%20membrane%20adsorbent%20is%20made,filtration%20performance%20of%20the%20membrane.)
**Highlights:**
* Application of polymeric membranes for the adsorption of hazardous pollutants may lead to the development of next-generation reusable and portable water purification appliances. **Membranes for membrane adsorption (MA) have the dual function of membrane filtration and adsorption to be very effective to remove trace amounts of pollutants such as cationic heavy metals, anionic phosphates and nitrates.** [\[Paper\]](https://link.springer.com/article/10.1007/s13201-018-0661-6)
* High performance nanofiltration (NF) membranes for heavy metal removal have been molecularly designed by adsorption of chelating polymers containing negatively charged functional groups such as poly (acrylic acid-co-maleic acid) (PAM), poly (acrylic acid) (PAA) and poly (dimethylamine-co-epichlorohydrin-co-ethylenediamine) (PDMED) on the positively charged polyethyleneimine (PEI) cross-linked P84 hollow fiber substrates. **Not only do these chelating polymers change the membrane surface charge and pore size, but also provide an extra mean to remove heavy metal ions through adsorption in addition to traditional steric effect and Donnan exclusion.** The adsorbed membranes have comparable water permeability and superior rejections to heavy metals, for instance, Pb(NO 3 ) 2 , CuSO 4 , NiCl 2 , CdCl 2 , ZnCl 2 , Na 2 Cr 2 O 7 and Na 2 HAsO 4 , with rejections higher than 98%. The membranes also display excellent rejections to mixed ions with rejections more than 99%. The newly developed membranes show reasonably stability during 60-h tests as well as multiple washes. [\[Art. #ARTNUM\]](#article-96282-2066359298)
| 5.6.1 | Membrane adsorption |
|---|---|
| Chelating polymer modified P84 nanofiltration (NF) hollow fiber membranes for high efficient heavy metal removal | |
| Abstract High performance nanofiltration (NF) membranes for heavy metal removal have been molecularly designed by adsorption of chelating polymers containing negatively charged functional groups such as poly (acrylic acid-co-maleic acid) (PAM), poly (acrylic acid) (PAA) and poly (dimethylamine-co-epichlorohydrin-co-ethylenediamine) (PDMED) on the positively charged polyethyleneimine (PEI) cross-linked P84 hollow fiber substrates. Not only do these chelating polymers change the membrane surface charge and pore size, but also provide an extra mean to remove heavy metal ions through adsorption in addition to traditional steric effect and Donnan exclusion. The adsorbed membranes have comparable water permeability and superior rejections to heavy metals, for instance, Pb(NO 3 ) 2 , CuSO 4 , NiCl 2 , CdCl 2 , ZnCl 2 , Na 2 Cr 2 O 7 and Na 2 HAsO 4 , with rejections higher than 98%. The membranes also display excellent rejections to mixed ions with rejections more than 99%. The newly developed membranes show reasonably stability during 60-h tests as well as multiple washes. | |
| 10/01/2014 00:00:00 | |
| Link to Article | |
5.7 biomembrane
Biomembranes are membranes from biological sources, such as eggshell membranes, nanocellulose (bacterial) etc.
**Highlights:**
* **Eggshell membrane (ESM) was selected and modified to adsorb heavy metals. Adsorption of metal ions on the modified ESM (MESM) might be attributed to electrostatic interaction, ion exchange and coordination effect with chelating ligands containing N and S on the surface of the MESM.** [ \[Art. #ARTNUM\]](#article-96087-2890836740)
* Here, we demonstrate a **novel membrane composed of polydopamine (PDA) particles and bacterial nanocellulose (BNC), which can efficiently remove a variety of metal ions and organic dyes from contaminated water.** The biocompatible and biodegradable PDA/BNC membrane is synthesized by in situ incorporation of PDA particles into BNC matrix during its bacteria-mediated growth. We show that the PDA/BNC membrane can effectively remove heavy metal ions such as lead and cadmium, and organic dyes as surrogate markers of organic pollutants such as rhodamine 6G (R6G), methylene blue (MB), and methyl orange (MO). The removal efficiencies of contaminants were tested separately or simultaneously via simple filtration at pH values ranging from 4 to 7. [\[Art. #ARTNUM\]](#article-96087-2910415304)
| 5.7.1 | biomembrane |
|---|---|
| A Robust and Scalable Polydopamine/Bacterial Nanocellulose Hybrid Membrane for Efficient Wastewater Treatment | |
| Toxic heavy metal ions and organic pollutants are significant concerns in wastewater treatment. Here, we demonstrate a novel membrane composed of polydopamine (PDA) particles and bacterial nanocellulose (BNC), which can efficiently remove a variety of metal ions and organic dyes from contaminated water. The biocompatible and biodegradable PDA/BNC membrane is synthesized by in situ incorporation of PDA particles into BNC matrix during its bacteria-mediated growth. We show that the PDA/BNC membrane can effectively remove heavy metal ions such as lead and cadmium, and organic dyes as surrogate markers of organic pollutants such as rhodamine 6G (R6G), methylene blue (MB), and methyl orange (MO). The removal efficiencies of contaminants were tested separately or simultaneously via simple filtration at pH values ranging from 4 to 7. Furthermore, after simple washing with regeneration agents, the membrane can be reused multiple times without compromising its contaminant sorption ability and mechanical integrity.... | |
| 02/22/2019 00:00:00 | |
| Link to Article | |
| 5.7.2 | biomembrane |
| Adsorption of heavy metal with modified eggshell membrane and the in situ synthesis of Cu–Ag/modified eggshell membrane composites | |
| The objectives of this study were to remove heavy metals from wastewater through the biosorption method with modified biomass as an effective sorbent and to prepare metal/biomass composites with the same modified biomass as a direct template. Eggshell membrane (ESM) was selected and modified to adsorb heavy metals. Adsorption of metal ions on the modified ESM (MESM) might be attributed to electrostatic interaction, ion exchange and coordination effect with chelating ligands containing N and S on the surface of the MESM. The pH of the solution was a key factor affecting the adsorption. The Cu–Ag/MESM composites with uniform Cu–Ag NPs were prepared with MESM as matrices, and with Cu 2+ and Ag + adsorbed as metal sources. The Cu–Ag/MESM showed excellent catalytic performance in the reduction of 4-nitrophenol to 4-aminophenol in the aqueous phase. Because of the high stability of the Cu–Ag NPs supported on the macro-dimension supporter, Cu–Ag/MESM can be easily separated after the catalytic reaction and recycled. | |
| 09/01/2018 00:00:00 | |
| Link to Article | |
6. Others
BackOther technologies
6.1 Photocatalysis
Photocatalysis is a type of catalysis that results in the modification of the rate of a photoreaction - a chemical reaction that involves the absorption of light by one or more reacting species - by adding substances (catalysts) that participate in the chemical reaction without being consumed.[\[Source\]](https://www.nature.com/subjects/photocatalysis#:\~:text=Photocatalysis%20is%20a%20type%20of,chemical%20reaction%20without%20being%20consumed.)
**Highlights:**
* With the help of semiconductor, photocatalytic process has caused considerable attention in removing heavy metal in wastewater for its high efficiency and rapid destruction. As generally observed, titanium dioxide can obtain the best photocatalytic performances. Upon of illumination of semiconductor-electrolyte, electron-hole pairs are formed in the conduction and the valence band of the semiconductor, respectively. Migrating to the surface of titanium dioxide, these charge carriers have redox potential. The hydroxylions (OH-) likely leads to the formation of hydroxyl radicals which has strong oxidizing property. And the traps for electrons are adsorbed oxygen species at the same time.[\[Art. #ARTNUM\]](#article-96288-2421754045)
* Based on biosorption and photodegradation coupling technology, a novel adsorbent, which not only adsorbs the heavy metal ions but also degrades organic compound, was prepared by immobilization of nano-TiO2 on chitosan matrix. [\[Art. #ARTNUM\]](#article-96288-2147241663)
| 6.1.1 | Photocatalysis |
|---|---|
| Degradation characteristic of TiO2-chitosan adsorbent on Rhodamine B and purification of industrial wastewater | |
| Based on biosorption and photodegradation coupling technology, a novel adsorbent, which not only adsorbs the heavy metal ions but also degrades organic compound, was prepared by immobilization of nano-TiO2 on chitosan matrix. Degradation characteristic of Rhodamine B (Rh.B) was investigated by TiO2-chitosan adsorbents. The results showed that degradation ratio reached 94.3% by 0.2 g adsorbents under ultraviolet radiation light (UV) at initial Rh.B concentration of 10 mg/L and optimal pH of 9.0. Degradation and adsorption behavior characteristics were discussed in the presence of binary pollutants (Rh.B and Ag+). The coexistence of Ag+ intensely inhibited the degradation ability of Rh.B. Higher Ag+ concentration weakened the degradation ability. However, Rh.B did not affect the adsorption capacity of Ag+. Moreover, TiO2-chitosan adsorbent contributed to a higher degradation ability of organic pollutants in practical wastewater. Degradation capacity of contaminants in paper-making wastewater reached 60.8 mg/g at the initial COD concentration of 2,000 mg/L. | |
| 05/01/2011 00:00:00 | |
| Link to Article | |
| 6.1.2 | Photocatalysis |
| New trends in removing heavy metals from wastewater. | |
| With the development of researches, the treatments of wastewater have reached a certain level. Whereas, heavy metals in wastewater cause special concern in recent times due to their recalcitrance and persistence in the environment. Therefore, it is important to get rid of the heavy metals in wastewater. The previous studies have provided many alternative processes in removing heavy metals from wastewater. This paper reviews the recent developments and various methods for the removal of heavy metals from wastewater. It also evaluates the advantages and limitations in application of these techniques. A particular focus is given to innovative removal processes including adsorption on abiological adsorbents, biosorption, and photocatalysis. Because these processes have leaded the new trends and attracted more and more researches in removing heavy metals from wastewater due to their high efficency, pluripotency and availability in a copious amount. In general, the applicability, characteristic of wastewater, cost-effectiveness, and plant simplicity are the key factors in selecting the most suitable method for the contaminated wastewater. | |
| 08/01/2016 00:00:00 | |
| Link to Article | |
6.2 Hydrocyclone
A hydrocyclone is a device to classify, separate or sort particles in a liquid suspension based on the ratio of their centripetal force to fluid resistance. This ratio is high for dense and coarse particles, and low for light and fine particles.[\[Wiki\]](https://en.wikipedia.org/wiki/Hydrocyclone)
**Highlights:**
* Heavy metals usually aggregate as fine particles in dredging slurry and need to be removed or reduced before recycling of the slurry. However, traditional hydrocyclone method often leads to low separation efficiency because of the difficulties in the complete separation of fine particles. To address this problem**, this paper proposes a new type of parabolic hydrocyclone for the removal of heavy metals from dredging slurry.** Therefore, after the parabolic hydrocyclone separation process, the underflow products contain less heavy metals and become both non-hazardous and recyclable. [\[Paper\]](https://www.revistascca.unam.mx/rica/index.php/rica/article/viewFile/RICA.2019.35.esp01.09/46853)
6.3 eutectic freeze crystallization
The basis of the Eutectic Freeze Crystallization (EFC) technology is the existence of the eutectic point. The eutectic point is a characteristic point in the phase diagram of a salt-water mixture. At the eutectic point an equilibrium exists between ice, salt and a solution with a specific concentration. This specific concentration is called the eutectic concentration and the temperature at which this equilibrium is found is the eutectic temperature.[\[Source\]](https://www.coolseparations.nl/efc-technology-how-it-works/#:\~:text=The%20basis%20of%20the%20Eutectic,solution%20with%20a%20specific%20concentration.)
**Highlights:**
* This paper focuses on the application of EFC for the purification of a typical brine containing high levels of sodium, chlorine, sulphate and ammonia that cannot be achieved with other separation techniques. The presence of ammonia prevents the application of membrane technology to treat the brine, leaving only cooling or evaporation as other possible options. Evaporation produces a mixed salt that requires further treatment. Modelling tools were applied to describe the phase behaviour of the complex saline systems under different process conditions and were experimentally validated. The results showed that Eutectic Freeze Crystallization could be used to selectively recover the sodium as a sodium sulphate salt. The simulation tools were especially useful in the design and optimisation of the process.[\[Paper\]](https://www.sciencedirect.com/science/article/abs/pii/S0263876210000377)
Final Results
Published 07/15/2020
After the midway results meeting, 10 inorganic contaminant removal technologies have been reviewed and deepened. The results are organised based on the concept and presented per inorganic contaminant removal technologies comprising a description, findings, suppliers (if applicable), images, videos, useful links and a reference list. The technology requirements are measured and shown in the [requirements table](#requirements-table). By using the concept links below, you can quickly navigate to the concepts and their inorganic contaminant removal technologies descriptions.
Table of concepts:
| Technology | Ranking | Input (biomass/contaminant) | Selectivity | Scale of operation |
|---|---|---|---|---|
| 1.1 Activated carbon |
(
)
|
Wastewaters(municipal, metal), leachates, runoff [[Art. #ARTNUM]](#article-96075-2886258277),spent liquids (brewing), seawater; removes phosphates, nitrates [[Art. #ARTNUM]](#article-96075-2886258277), some heavy metals (Pb, Cu, Cd, Ni, Cr, Zn) [[paper]](https://link.springer.com/article/10.1007/s13201-016-0460-x#:~:text=The%20effect%20of%20temperature%20and,and%20Lead%20from%20the%20wastewater.), not suited for other salts (Fe, F, Al, Ca etc.) [[Source]](https://www.springwellwater.com/activated-carbon-filters-remove/) | Not very selective for inorganic contaminants, also phenolics and organic contaminants are removed. Slightly depedent on the type of activated carbon [[Paper]](https://www.researchgate.net/publication/277673886_Removal_of_Heavy_Metal_Ions_with_Acid_Activated_Carbons_Derived_from_Oil_Palm_and_Coconut_Shells) | Can be used on large scales, however, the larger the scale the larger the amount of Ac that is required. Granular activated filters are usually used on larger scales. |
| 1.2 Organic waste materials |
(
)
|
Wastewater (tannery, metal, industrial, municipal) [[Art. #ARTNUM]](#article-96093-2059870110), soil remediation. Mainly tested for heavy metals [[Art. #ARTNUM]](#article-96093-2059870110), also nitrates/ammonium[[Art. #ARTNUM]](#article-96093-2355542055) and chlorides [[Paper]](https://www.environmentaljournal.org/1-4/ujert-1-4-4.pdf) | Depends on kind of sorbent; quite selective for heavy metals usually, pretreatments can be done to improve selectivity. [[Paper]](https://www.researchgate.net/publication/262527665_New_Biosorbent_Materials_Selectivity_and_Bioengineering_Insights) | Pilot to full scale have been tested, commercial processes on large scales are still lacking [[Art. #ARTNUM]](#article-96093-2059870110) |
| 1.3 Biosorption |
(
)
|
Wastewater:aqueous solution. Mainly for heavy metals [[Art. #ARTNUM]](#article-96076-1523946948) ; [[Art. #ARTNUM]](#article-96076-2185808385) ; soils, sediments and water [[Art. #ARTNUM]](#article-96076-2783282207) | Can be highly selective depending on biomass. Some algae or fungi have sorption capacity for mainly (or one kind of) heavy metal | Needs to be produced on large scales. Waste from fermentations could be used. pilot scales have been done. [[Art. #ARTNUM]](#article-96076-2170889100) |
| 2.1 Electrocoagulation |
(
)
|
Wastewater (food, tannery, industrial, municipal, runoff, leachate), sludge ; Heavy metals, nutrients, (total dissolved solids) [[Art. #ARTNUM]](#article-96077-2203672557) | Selectvity is dependent on situation (contaminant, pH, temperature, electrodes); each new situation needs to be developed for selectivity.[[Art. #ARTNUM]](#article-96077-2203672557) | Large scale systems are possible. (2000L/h [[Morselt]](https://www.morselt.com/en/products/wastewater-treatment.html); 100KL/day [[R&T Eco]](https://www.rteco.in/electrocoagulation-electroflotation-reactor) |
| 3.1 Bioleaching |
(
)
|
wastewater, sludge, soil ; heavy metals, nutrients (phosphate, nitrate) [[Art. #ARTNUM]](#article-96079-91473926) ; [[Art. #ARTNUM]](#article-96079-1418464678) ; [[Art. #ARTNUM]](#article-96079-2048449249) | Some microorganisms are very selective for one contaminant (also one specific heavy metal), but they also usually take up nutrients and some organics [[Art. #ARTNUM]](#article-96079-2792853950) | Large scales possible. They usually take long times (days). [[Art. #ARTNUM]](#article-96079-2359122416) |
| 4.1 ultrafiltration |
(
)
|
Wastewater, heavy metals [[Art. #ARTNUM]](#article-96074-2611225203) | When enhanced it can be quite selective for certain contaminants [[Art. #ARTNUM]](#article-96074-2922823182) | Large scale possible, but especially enhanced UF is still under development |
| 4.2 nanofiltration (NF) |
(
)
|
Wastewater, mainly phosphaste, nitrate [[Art. #ARTNUM]](#article-96121-2000756297), chloride [[Art. #ARTNUM]](#article-96121-2324824251). Also heavy metals [[Art. #ARTNUM]](#article-96121-2324815137), usually requires pre-treatment [[Paper]](https://www.intechopen.com/books/wastewater-and-water-quality/wastewater-treatment-using-membrane-technology). | Can have high removal efficiency for salts and metals, largely dependent on membrane and waste stream [[Paper]](https://www.intechopen.com/books/wastewater-and-water-quality/wastewater-treatment-using-membrane-technology) | Composites that can deal with fouling are largely still under development. |
| 4.3 Reverse osmosis |
(
)
|
Needs pretreatment usually for wastewater [[Paper]](https://www.intechopen.com/books/wastewater-and-water-quality/wastewater-treatment-using-membrane-technology); heavy metals [[Art. #ARTNUM]](#article-96290-2311502662), ammonia, salts, nitrates, phosphate [[Art. #ARTNUM]](#article-96290-2803370931) | Removes solutes in general; can be ion-selective | expensive membranes, so especially expensive at large scales; need pretreatment ; 10,000 gals per day of leachate [[dynatec]](http://www.dynatecsystems.com/index.asp?PageID=204) |
| 4.4 Electrodialysis |
(
)
|
Wastewater/sludge (with water) [[Art. #ARTNUM]](#article-96117-1980378680), [[Art. #ARTNUM]](#article-96117-2043219105); heavy metals [[Art. #ARTNUM]](#article-96117-1980378680), ammonia [[Art. #ARTNUM]](#article-96117-2907165361), phosphate [[Art. #ARTNUM]](#article-96117-2241515304), salts. | Can be more selective than other membrane separations, because of the ion exchange membrane. [[Art. #ARTNUM]](#article-96117-2947013546) | Large scale possible (150 m3/h [[Suez]](https://www.suezwatertechnologies.com/products/edediedr/electrodialysis-reversal-edr) |
| 4.5 Membrane adsorption |
(
)
|
Waste water ; Heavy metals, phosphates. [[Art. #ARTNUM]](#article-96282-2066359298), [[Art. #ARTNUM]](#article-96282-2791240048) | Usually the specific sorption is used for selective removal of certain components ; n [[Art. #ARTNUM]](#article-96282-2791240048) | usually membranes are more complex, still under development |
1. Sorption materials
BackMaterials that ab/adsorb contaminants physically or chemically.
1.1 Activated carbon
Activated carbon, also called activated charcoal, is a form of carbon processed to have small, low-volume pores that increase the surface area available for adsorption or chemical reactions.[\[Wiki\]](https://en.wikipedia.org/wiki/Activated_carbon#:\~:text=Activated%20carbon%2C%20also%20called%20activated,is%20sometimes%20substituted%20with%20active.)
**Contaminants:**
* Activated carbon filters are efficient to remove certain organics (such as unwanted taste and odours, micropollutants), chlorine, fluorine or radon, from drinking water or wastewater. However, it is not effective for microbial contaminants, metals, nitrates and other inorganic contaminants.[\[Source\]](https://sswm.info/sswm-university-course/module-6-disaster-situations-planning-and-preparedness/further-resources-0/adsorption-%28activated-carbon%29#:\~:text=Activated%20carbon%20filters%20are%20efficient,nitrates%20and%20other%20inorganic%20contaminants.)
* **Without unique materials or additional filtration**, activated carbon won’t filter:
* Radionuclides
* Most microbiological contaminants, including bacteria, viruses, cysts, coliform, protozoa, and other microorganisms
* Significant amounts of heavy metals, copper, or iron
* Inorganic pollutants like asbestos, and arsenic
* Healthy minerals, such as calcium, potassium, and magnesium
* Significant amounts of hydrocarbons or petroleum distillates
* Dissolved solids, including minerals, salts, or metals, such as iron that aren’t usually considered contaminants. [\[Source\]](https://www.springwellwater.com/activated-carbon-filters-remove/)
* **Granular Activated Carbon (GAC)**: During a second stage, filtration through GAC will result in a satisfactory reduction of unwanted or toxic ions. Silver and mercury will be totally removed while lead and copper levels (excluding nickel) will fall below the guidelines set. [\[Source\]](https://www.watercare.co.uk/heavy-metal-removal/)
* For example, sodium, microbes, fluoride, and nitrates cannot be removed with AC filtration. Water softening also cannot be achieved with AC filters. In addition, heavy metals, such as lead, can only be removed with a **very specific kind of activated carbon water treatment**, which is typically used only in residential point-of-use filters. [\[Source\]](https://www.waterprofessionals.com/learning-center/activated-carbon-filters/)
However, ACs can be treated in different ways to also adsorb significant amounts of heavy metals and/or nutrient. ACs from different sources (sludge or biobased materials, also have different selectivities).
**Highlights:**
* The effect of temperature and contact time on the removal of these heavy metals using the activated carbon produced was investigated. The activated carbon showed a significant ability in removing heavy metals; Cadmium, Copper, Nickel, and Lead from the wastewater. [\[Paper\]](https://link.springer.com/article/10.1007/s13201-016-0460-x#:\~:text=The%20effect%20of%20temperature%20and,and%20Lead%20from%20the%20wastewater.)
* Batch experiments were conducted to test the ability of activated carbon for the removal of lead, cadmium, nickel, chromium and zinc from water. Nickel showed the highest removal percentages by activated carbon at all concentrations and the removal percentages decreased as the concentration of heavy metal increased. [\[Paper\]](https://www.sciencedirect.com/science/article/pii/S1876610214007504)
* Nutrients (P, N) in stormwater runoff are a major cause of eutrophication and algal blooms. **A promising solution to this problem is to amend the rain garden growing medium (RGGM) with sewage sludge-based activated carbon (SBAC).** To optimize the SBAC production process, different metals, pyrolysis conditions (temperature, heating time, carrier gas), and post-treatments were explored. When pyrolyzed at 400 °C for two hours, Zn-activated SBAC removed up to 41% of PO4-P (initial concentration of 1 mg/L) and 72% of NO3-N (initial concentration of 2 mg/L), at a dose of 1 g sorbent/L of nutrient-spiked distilled water. When the same dosage was applied to stormwater leachate made from RGGM and spiked with nutrients, the removal efficiencies were reduced to 20% for PO4-P and 38% for NO3-N. [\[Art. #ARTNUM\]](#article-96075-2886258277)
* Carbon’s **de-chlorinating** capability results from its ability to act as a reducing agent that reacts with strong oxidising agents such as chlorine dioxide and hypochlorous acid. **It reduces a wide variety of organic contaminants and can be designed to reduce levels of some inorganic chemicals like lead and arsenic.** However, activated carbon is ineffective against many inorganic contaminants such salts, iron, fluoride, aluminium and calcium. [\[Art. #ARTNUM\]](#article-96075-2316625256)
* In this work, batch adsorption experiments were carried out to investigate the suitability of prepared **acid activated carbons in removing heavy metal ions** such as nickel(II), lead(II) and chromium(VI). Prepared activated carbons showed higher adsorption capacity for nickel(II) and lead(II). The removal of chromium(VI) was studied by the prepared acid activated, modified and commercial activated carbons at different pH. The commercial activated carbon has some limitations because of its lower adsorption capacity in the low concentration range. Hence, it cannot be suitable for drinking water purification. In contrast, **acid activated carbon has the potential to scavenge some heavy metal cations and anions completely in low concentration which indicates its stronger affinity towards all heavy metal ions.** **Phosphoric acid activation forming surface acidic groups thus produces activated carbon suitable for removing heavy metal ions.** [\[Paper\]](https://www.researchgate.net/publication/277673886_Removal_of_Heavy_Metal_Ions_with_Acid_Activated_Carbons_Derived_from_Oil_Palm_and_Coconut_Shells)
* In this study, **the effectiveness of activated carbon absorbents obtained from pyrolysis of rice husk on nitrate adsorption is explored**, and the results of the adsorption by carbon prepared from primary sludge of wastewater treatment of paper industry have been compared. The maximum removal of nitrate for activated carbon obtained from rice husk was 93.5 (mg/gr), and for the sludge obtained from paper industry was 79.5 (mg/gr). The result of tests for both adsorbents suggests a direct relationship between the level of adsorption run by Zncl2 used to activate adsorbents and the level of adsorbent.[\[Paper\]](https://www.researchgate.net/publication/303613211_Removal_of_Nitrate_from_Ground_Water_Using_Activated_Carbon_Prepared_from_Rice_Husk_and_Sludge_of_Paper_Industry_Wastewater_Treatment)
* This article reports a series of commercially prepared specifically modified activated carbons based on ionic organic modifiers or chelates added at 10–15% of the total weight of the sorbent, **designed for the removal of oxyanions such as chromate, arsenate, selenate, etc., or heavy metals as nickel, copper, zinc, cadmium, etc.** Sorbents were tested for chromium, arsenic, nickel and perchlorate, and complete removal of pollutant was observed for hundreds to thousands of bed volumes depending on the pollutant concentrations. [\[Paper\]](https://www.researchgate.net/publication/233733192_Functionalized_activated_carbons_for_the_removal_of_inorganic_pollutants)
* The highest efficiency of nitrate removal (95.4%) was related to application of modified activated carbon to a solution with pH of 7 and 100 mg L^−1^ nitrate concentration.[\[Paper\]](https://iwaponline.com/ws/article/19/4/1097/64198/Nitrate-removal-from-water-using-complex-of)
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| 1.1.1 | Activated carbon |
|---|---|
| Adsorptive Treatment of Landfill Leachate using Activated Carbon Modified with Three Different Methods | |
| Activated Carbon (AC) is an adsorbent having high surface area which makes the process of removing heavy metals from wastewater (such as landfill leachate) very effective. This study explored the utilization of three methods of modification of AC produced from coconut shell by treating it with nitric acid (HNO3), potassium permanganate (KMnO4) and heating at 600°C to improve the adsorption capacity. The AC can remove multi-pollutants in the filtration process which was used to treat landfill leachate. The water quality parameters such as pH, TSS, Ammonia-Nitrogen and a few heavy metals were considered in the present study. Results showed that the removal of these parameters was proportional with the increase of contact time and the bed depth of AC. The isotherm analysis of the adsorption of modified AC showed the best Removal Efficiency (RE) can be achieved when AC treated with KMnO4 for NH3-N, zinc, TSS and sulphide. The morphology of the AC was studied through Scanning Electron Microscopy (SEM), Energy Dispersive X-ray spectroscopy (EDX) pattern analysis and Fourier Transform Infrared (FTIR) analysis. It was found that various types of oxygen functional groups were introduced onto the surface of coconut shell derived AC through oxidation using HNO3. FTIR was used to characterize the surface oxygen functional groups. The surface functional groups such as N-H and C-H stretching played a significant role in heavy metals adsorption. Hence, it can be concluded that the hybrid technique by using electrolysis process with AC adsorption be an effective way to remove the suspended solids and heavy metals from landfill leachate and thus able to reduce environmental pollution. | |
| 04/01/2018 00:00:00 | |
| Link to Article | |
| 1.1.2 | Activated carbon |
| Aerobic sludge granulation facilitated by activated carbon for partial nitrification treatment of ammonia-rich wastewater | |
| Abstract Although the use of partial nitrification, or nitritation, for nitrogen removal via nitrite is an energy-saving method for treating high-strength ammonia wastewater, its stable operation with sufficient enrichment of ammonia-oxidizing bacteria (AOB) is difficult to maintain in activated sludge systems. In this study, an aerobic granulation technique was developed for the effective and stable nitritation treatment of ammonia-rich inorganic influent. Granular activated carbon (GAC) or powdered activated carbon (PAC) was added to the bioreactor to enhance the granulation of slow-growing AOB. The results show that aerobic granules could be formed for partial nitrification through the selective discharge of small and slow-settling sludge flocs, with or without activated carbon addition. However, dosing GAC into the sludge greatly accelerated the granulation process and shortened the granulation period from about 6 weeks to less than 3 weeks with the formation of large and fast-settling granules. In contrast, dosing PAC led to the slower formation of smaller granules. Compared to activated sludge flocs, sludge granulation with selective sludge discharge was found to help halt ammonia oxidation to the level of partial nitrification rather than complete nitrification. Based on the molecular analysis, aerobic granulation resulted in AOB enrichment and the reduction of nitrite-oxidizing bacteria (NOB) in granules, which is highly favorable to a stable partial nitrification operation. | |
| 02/01/2013 00:00:00 | |
| Link to Article | |
| 1.1.3 | Activated carbon |
| Biosorption of Heavy Metal by Algae Biomass in Surface Water | |
| Discharging wastewater containing heavy metals of Cu, Pb, Zn and Cd into water bodies can cause toxicity in plants and aquatic animals and some of them will be unable to survive except algae. Wastewater treatment method to remove heavy metal contaminants includes chemical precipitation, ion exchange, membrane, filtration, adsorption using activated carbon. However, these methods are either expensive or have other disadvantages such as high energy consumption and inefficiencies when existing heavy metals are at trace concentration. Biosorption using algae biomass can be an alternative method to eliminate heavy metals. The objective of the project is to investigate the capability of Marine Algae (MA) and Freshwater Algae (FA) bi-omass in adsorbing heavy metals of Cu, Pb, Zn and Cd from water medium using synthetic water and industrial water. MA and FA were obtained from the eastern coast of Pulau Ubin and local fish farm respectively. After being fully washed with deionised water, dried in a furnace for 105°C, they are grinded to pass 1 mm2 of siever. MA and FA were characterised using FTIR to determine their functional groups. An industrial water was collected from industrial discharge from metal fac-tories in northern side of Singapore. Effect of adsorption time, adsorbent concentra-tion, and pH were studied. The result showed that FA and MA had a higher capability in adsorbing a total metal of about 40 ppm level from an industrial water, or 4 times than synthetic water concentration, at the same adsorbent dosage of 50 mg. In con-clusion, the presence of various functional groups, hydroxyl, carboxylic and amine groups, in all MA and FA samples had enabled the algae biomass to adsorb heavy metals of Cu, Pb, Cd and Zn from synthetic and industrial water. Due to their bio-sorptive properties and fast adsorption capability, algae could be a potential method for cleaning up surface water or post-treatment of wastewater and minimise the cost of eutrophication. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 1.1.4 | Activated carbon |
| Effect of powdered activated carbon technology on short-cut nitrogen removal for coal gasification wastewater. | |
| A combined process consisting of a powdered activated carbon technology (PACT) and short-cut biological nitrogen removal reactor (SBNR) was developed to enhance the removal efficiency of the total nitrogen (TN) from the effluent of an upflow anaerobic sludge bed (UASB) reactor, which was used to treat coal gasification wastewater (CGW). The SBNR performance was improved with the increasing of COD and TP removal efficiency via PACT. The average removal efficiencies of COD and TP in PACT were respectively 85.80% and 90.30%. Meanwhile, the NH3–N to NO2–N conversion rate was achieved 86.89% in SBNR and the total nitrogen (TN) removal efficiency was 75.54%. In contrast, the AOB in SBNR was significantly inhibited without PACT or with poor performance of PACT in advance, which rendered the removal of TN. Furthermore, PAC was demonstrated to remove some refractory compounds, which therefore improved the biodegradability of the coal gasification wastewater. | |
| 08/01/2013 00:00:00 | |
| Link to Article | |
| 1.1.5 | Activated carbon |
| Effectiveness of Raw versus Activated Coconut Shells for Removing Arsenic and Mercury from Water | |
| Relatively inexpensive biosorbents, made from coconut shell, were explored as alternatives to high-quality activated carbon for use in small-scale, wastewater treatment in developing economies. Simple charring and activation procedures were followed to produce CaCl2-activated coconut shell charcoal and its effectiveness was compared with raw coconut shell powder for removal of mercury (Hg) and arsenic (As) from contaminated water. From atomic absorption spectroscopy analyses, the removal efficiency of As and Hg with the use of activated charcoal were 67% (vs 65% for the raw form), and 53% (vs 49% for the raw form), respectively, from their corresponding “artificially”-contaminated wastewater. These results suggest that despite the slightly improved removal efficiencies recorded for activated coconut shells, the raw version could equally be used in treating wastewater towards the removal of the toxic metals- As and Hg. In order to understand the chemistry of the adsorption processes, FT-IR spectroscopy was employed to study similarities and differences in chemical compositions of the raw versus activated coconut shells before and after the biofiltration processes. To further investigate the effect of this biofiltration process on the overall quality of water, the physicochemical parameters (pH, conductivity, colour, turbidity, TDS and TSS) were measured on river water samples, pre-treated with the biosorbents. For both the raw and activated coconut shell, there was general improvement, although the conductivity of the water treated with the activated version was slightly elevated, was likely due to leaching of CaCl2 that was used for activation. | |
| 09/30/2019 00:00:00 | |
| Link to Article | |
| 1.1.6 | Activated carbon |
| Experimental Study on Heavy Metal Removal from Textile Industrial Wastewater Using Banana Peel and Activated Carbon from Coconut Shell as an Adsorbent | |
| The most important class of pollutants is the effluents (dyes) which are disposed directly to the river from the textile industries. This effluent contains several heavy metals like chromium and copper. Some of the heavy metals which are present in even smaller amount will cause a greater pollution. Disposal of the effluents into the water streams or precious water resource must be avoided. However there are various treatment methods before disposal, which will not be effective in the removal of heavy metals. Adsorption is recognized as an effective and economic method for low concentration heavy metal wastewater treatment. In the adsorption process numerous adsorbents are available. In this study, we used banana peel and activated carbon produced from coconut shell as a low cost adsorbent. A comparative study is done in order to make a comparison between the removal efficiency of chromium by these adsorbent. The dosage of adsorbents is about 10 grams, 15 grams, 20 grams which will create a situation of removing heavy metals. The adsorption process is done at the room temperature for about an hour for each adsorbent. The adsorption process is started with the initial concentration of 10 gram of each adsorbent and then gradually increased based on the removal percentage. At the end 25 gram of dosage is given beyond that which produces no change in the removal of heavy metals. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 1.1.7 | Activated carbon |
| Exploratory study on modification of sludge-based activated carbon for nutrient removal from stormwater runoff | |
| Abstract Nutrients (P, N) in stormwater runoff are a major cause of eutrophication and algal blooms. A promising solution to this problem is to amend the rain garden growing medium (RGGM) with sewage sludge-based activated carbon (SBAC). To optimize the SBAC production process, different metals, pyrolysis conditions (temperature, heating time, carrier gas), and post-treatments were explored. When pyrolyzed at 400 °C for two hours, Zn-activated SBAC removed up to 41% of PO 4 -P (initial concentration of 1 mg/L) and 72% of NO 3 -N (initial concentration of 2 mg/L), at a dose of 1 g sorbent/L of nutrient-spiked distilled water. When the same dosage was applied to stormwater leachate made from RGGM and spiked with nutrients, the removal efficiencies were reduced to 20% for PO 4 -P and 38% for NO 3 -N. These reductions were probably caused by competition from other leachate components. Increasing the dosage to 3 g/L leachate improved PO 4 -P removal to 31% and NO 3 -N to 72%, while also resulting in the removal of 46% of total organic carbon. The major energy cost of producing such sorbents is estimated to be ∼$0.76 CAD/kg SBAC. | |
| 11/01/2018 00:00:00 | |
| Link to Article | |
| 1.1.8 | Activated carbon |
| Immobilizing Microcystis aeruginosa and powdered activated carbon for the anaerobic digestate effluent treatment | |
| Abstract The environment pollution caused by livestock anaerobic digestate effluent (ADE) is becoming increasingly severe recently. In this study, immobilized technology, embedding Microcystis aeruginosa (MA) and powdered activated carbon (PAC) with sodium alginate (SA), was employed to investigate the removal performance of nitrogen (TN), phosphorus (TP) and dissolved organic matter (DOM) in the treatment of ADE solution. Initially, orthogonal experiment was carried out to achieve the optimal conditions of the beads fabrication with the concentration of imbedding agents (PAC-SA) of 5% (w/w) and the ratio of microalgae and imbedding agents was 1:1 (v/v). The results indicated that the total nitrogen (TN), total phosphorus (TP) and total organic carbon (TOC) can be efficiently removed under the optimal operation conditions, with average removals of 91.88 ± 2.91% in TN, 98.24 ± 0.12 in TP and 78.31 ± 1.57% in TOC, respectively. Moreover, the fluorescence excitation-mission matrix (EEM) results illustrated that IMA-PAC beads joined system can efficiently diminish the concentrations of protein-like compounds and humic substances. Therefore, the organic contaminants and nutrients (i.e. N and P) can be efficiently removed in IMA-PAC beads joined system, which would contribute to developing new strategies for the treatment of ADE solution and nutrient recycle. | |
| 04/01/2020 00:00:00 | |
| Link to Article | |
| 1.1.9 | Activated carbon |
| Investigation of municipal and olive mill wastewater co-treatment in activated sludge - powdered activated carbon (AS-PAC) systems | |
| BACKGROUND: The purpose of this study was to investigate the co-treatment of olive-mill wastewater (OMW) and municipal wastewater in activated sludge systems operating in the absence and presence of different adsorbent materials and to study the role of sorption and biodegradation in total phenols removal. RESULTS: Batch experiments were initially conducted to investigate total phenols’ adsorption capacity on activated sludge (AS), olive pomace (OP) and powdered activated carbon (PAC). According to the results, PAC presented the best adsorption capacity. Three sequencing batch reactors (SBRs) were also operated, treating municipal wastewater and different amounts of OMW. The first SBR contained AS (AS-System), the second AS and OP (AS-OP System) and the third AS and PAC (AS-PAC System). All SBRs operated sufficiently in the presence of 1% v/v OMW, achieving mean COD and total phenols removal efficiency higher than 86% and 85%, respectively, and satisfactory settling capacity. Increase of OMW concentration to 5% v/v affected the performance of SBRs, resulting in mean COD removal efficiencies that ranged between 61% (AS-OP System) and 80% (AS-PAC System). CONCLUSION: Among the SBRs used, the AS-PAC System operated with highest performance in the presence of 1 and 2.5% v/v OMW, and showed better stability in the presence of 5% v/v OMW. Calculation of total phenols mass flux revealed that biodegradation was the principal mechanism of their removal. The highest values of mean biotransformation rates were calculated for the AS-PAC System and ranged between 2.0 and 40.6 d −1 for different experimental phases. c � 2012 Society of Chemical Industry | |
| 04/01/2012 00:00:00 | |
| Link to Article | |
| 1.1.10 | Activated carbon |
| Mechanism of high contaminant removal performance in the expanded granular sludge blanket (EGSB) reactor involved with granular activated carbon for low-strength wastewater treatment | |
| Abstract The sludge granulation in an anaerobic bioreactor is rather difficult for treating low-strength wastewater. In this study, an expanded granular sludge blanket (EGSB) reactor involved with granular activated carbon (GAC) was employed to treat wastewater at different operational conditions. In general, a stable COD removal performance was operated at the HRT condition of 8, 6, 5, and 4 h, and V up ranges from 1.09 to 2.44 m h −1 . However, the NH 3 -N removal efficiency was at a relatively low level resulted from the nitrification efficiency was limited to the low dissolved oxygen concentration in anaerobic bioreactor. Adding GAC to the raw sludge, the average size of granular sludge and enzymatic [dehydrogenase activity (DHA) and specific methanogenic activity (SMA)] activities presented an increase trend with the experiment grows. In addition, the promotion of organic load rate (OLR) and V up might stimulate the external mass transfer effect in EGSB reactor, which resulted in the increase of extracellular polymeric substances (EPS) content. DNA sequencing analysis demonstrated that the growth of Aeromonas genus was the main reason for the unstable distribution of acetoclastic and hydrogenotrophic methanogens in HRT condition of 4 h. | |
| 02/01/2018 00:00:00 | |
| Link to Article | |
| 1.1.11 | Activated carbon |
| Selective removal of heavy metals from landfill leachate by reactive granular filters | |
| Abstract The pre-treatment of landfill leachate prior to its co-treatment in the municipal plants of waste water processing could represent an appropriate and cost-effective solution for its management. Pre-treatment is necessary especially to remove heavy metals, which may be transferred to the excess sludge preventing its valorisation. In the present paper, we propose a chemical-physical pre-treatment of leachate using four different granular reactive media able to selectively remove the contaminants present in the leachate. The efficiency of these materials was investigated using synthetic leachate through batch tests and a column test. In the latter case the four materials were placed in two columns connected in series and fed an under constant upward flow (0.5 mL/min). The first column was filled half (50 cm) with a granular mixture of zero valent iron (ZVI) and pumice and half (50 cm) with a granular mixture of ZVI and granular activated carbon (GAC). The second column, which was fed with the effluent of the first column, was filled half with zeolite (chabazite) and half with GAC. Heavy metals were mainly removed by the ZVI/pumice and ZVI/GAC steps with a removal efficiency that was higher than 98, 94 and 90% for copper, nickel and zinc, respectively, after 70 days of operation. Ammonium was removed by zeolite with a removal efficiency of 99% up to 23 days. The average reduction of the chemical oxygen demand (COD) was of 40% for 85 days, whereas chloride and sulphate removal was negligible. | |
| 12/01/2018 00:00:00 | |
| Link to Article | |
| 1.1.12 | Activated carbon |
| Study on the removal of heavy metal ions from industry waste by carbon nanotubes: Effect of the surface modification: a review | |
| AbstractRemoval of noxious materials such as heavy metal ions (which are hazardous above certain ppm concentration) from wastewater is one of the biggest environmental challenges that suffers the economy nowadays. On the basis of their versatility, environmental friendliness, the adsorption was proved to be a most economical and efficient technology, which is used extensively for their removal from the aqueous media. Among the various developed adsorbents used so far, carbon nanotubes (CNTs) show a unique impact on the fast adsorption and rapid removal of noxious impurities from the aqueous source. CNTs festooned on the sources like activated carbon, nanoparticles, and nanocomposities enhanced the efficiency and potential of the adsorbent. Due to their unique structural, electronic, optoelectronic, semiconductor, as well as mechanical, chemical, and physical properties, they have been extensively used to remove heavy metals in wastewater treatment. The adsorption mechanisms are majorly contributed by the ... | |
| 01/17/2016 00:00:00 | |
| Link to Article | |
| 1.1.13 | Activated carbon |
| The Effect of Microbial Population and Bioregeneration of used GAC in an Activated Sludge Reactor | |
| In the present work an attempt is made to study the role of microbial population on bioregenerationof granular activated carbon (GAC) loaded with phenol compounds in continues bioreactor. The GAC used to treat industrial wastewater of the Mobarakeh steel factory (EsfahanIran), is regenerated by means of biological method. Industrial microbes that obtained from the chemical wastewater treatment unit (in the Mobarakeh steel factory), were used in the bioregeneration process of activated carbon. The relationships between each two important parameters of bioregeneration such as adsorbed phenol, pH, mixed liquor suspended solids (MLSS), total suspended solids (TSS) and sludge volume index (SVI) were studied. It was observed that the adsorption capacity of the bioregenerated GAC increased during the two months of bioregeneration. Furthermore, it was found that pH gradually decreased with degradation of chemical compounds within pores of used GAC. The phenol adsorption capacity increased with increasing microbial cells concentration. In addition, the sludge volume index (SVI) decreased from around 231.11 mL mg -1 to 32.68 mL mg -1 during two months of bioregeneration of used GAC. While microbial concentration increases during thebioregeneration process in continues bioreactor. | |
| 12/22/2012 00:00:00 | |
| Link to Article | |
| 1.1.14 | Activated carbon |
| The Efficiency of Cactus Leaves and Wood Charcoal as a Potential Low-Cost Adsorbent for Removal of Toxic Heavy Metals from Industrial Effluents | |
| Presence of toxic heavy metals in the environment is of great concern due to their persistence in nature and chronic adverse effects on human health and the environment. Present paper tries to evaluate the efficiency of cactus leaves ( Opuntia f. indica ) and activated carbon made from acacia etbiaca as an adsorbent for the removal of heavy metal pollutants such as cadmium, lead and chromium from water. Adsorption properties such as size, dose, initial concentration and time of contact for cadmium, lead and chromium were studied through batch method. Before removing the toxic heavy metals (Cd, Pb and Cr), the fresh unpeeled cactus leaves (adsorbent) and activated carbon were washed with distilled water to eliminate the turbidity and smell from fresh unpeeled cactus. To describe the equilibrium isotherms, the experimental data were analyzed by the Langmuir and Freundlich isotherm models. Thus, the Freundlich model gave the best correlation with the experimental data. Therefore, the findings indicated that the cactus and activated carbon made locally from acacia etbiaca were found to be effective and low-cost alternative adsorbents for the removal of toxic heavy metals from industrial effluents. The preparation method allowed the use of these materials by local industries for effective remediation of pollution by removing heavy metals from their effluents. Keywords : Cactus leaves; Acacia etbiaca ; Heavy metals; Adsorption, Industrial effluents; Water purification. | |
| 02/15/2019 00:00:00 | |
| Link to Article | |
| 1.1.15 | Activated carbon |
| Treatment technology for brewery wastewater in a water-scarce country: A review | |
| Water is a scarce resource in many parts of the world; consequently the application of innovative strategies to treat wastewater for reuse is a priority. The brewery industry is one of the largest industrial users of water, but its effluent is characterised by high levels of organic contaminants which require remediation before reuse. Various conventional treatment methods such as anaerobic and aerobic systems, which are effective options because of their high removal efficiencies, are discussed in this study. Other methods such as membrane based technologies, carbon nanotubes, activated carbon, electrochemical methods, algal ponds and constructed wetlands are also analysed. Their efficiency as well as advantages and disadvantages are highlighted and evaluated. Combinations of various treatment processes to improve the quality of the final effluent are discussed. | |
| 03/30/2016 00:00:00 | |
| Link to Article | |
| 1.1.16 | Activated carbon |
| Zero-Wastewater Capacitive Deionization: Selective Removal of Heavy Metal Ions in Tap Water Assisted by Phosphate Ions | |
| Removing trace toxic heavy metals such as Pb2+ completely from drinking water is important for protecting human health. However, healthy ions such as Ca2+ and Mg2+ in reasonable concentrations are beneficial to human health and thus do not need to be removed. Here we report a zero-wastewater capacitive deionization (CDI) technology using a thiol-functionalized graphene oxide/activated carbon (GO/AC) composite material for the selective removal of heavy metal ions in tap water. The thiol groups have a strong affinity to heavy ions (such as Pb2+), leading to very high Pb removal selectivity against Ca2+ and Mg2+. More importantly, native phosphate ions were found to significantly modify the CDI process in tap water. The presence of phosphate ions leads to the formation of Pb particulates with free ions in the tap water. During charging the particulates are removed by electrosorption onto cathodes while the accumulated Pb particulates are released upon discharging, forming precipitates by reacting with concentrated phosphate ions from anodes. The precipitates can be subsequently collected using filters equipped in the pipeline, thereby leading to a zero-wastewater CDI. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
1.2 Organic waste materials
It is reported that there are many agricultural and biological wastes materials can be used as adsorbents for the removal of heavy metals from wastewater. **New resources such as rice husk, eggshell, Moringa pods, bamboo leaf powder, cashew nut shells, palm oil fruit shells, and barley straw show great capacity of heavy metal removal.**
Some biosorbents can also be used to remove nitrates or chloride, but the majority of research is on heavy metal remediation.
Selectivity is very dependent on the type of material and on the concentrations in the waste stream. It can be highly selective for only 1 contaminant, or be more general. Some pre-treatments, as well as engineering strategies exist to tailor this, which is a very active field of research. [\[Paper\]](https://www.researchgate.net/publication/262527665_New_Biosorbent_Materials_Selectivity_and_Bioengineering_Insights)
**Heavy metals:**
* The reviewed studies indicated that process conditions and parameters, such as pH, temperature, and contact time, need to be controlled in order to maximize the adsorption capacity. Biosorbents can be produced from different raw materials such as agricultural waste, food waste, industrial sludge and microbial cells (bacteria, fungi, and yeast). **The use of organic and agricultural waste as biosorbents is particularly promising, as there are already several cases where their effectivity for binding heavy metals has been demonstrated at the semi-industrial scales.** [\[Review\]](https://link.springer.com/article/10.1007/s40726-020-00135-7)
* And there are many materials which were studied including **Moringa pods**, **Bamboo leaf powder**, **Rice husk**, **palm fruit shells**, **okra waste**, **cashew nut shells**. [\[Paper\]](https://link.springer.com/article/10.1007%2Fs00253-016-7646-x)
* Trace amounts of toxic metalloids and heavy metals (HMs) would contaminate large volumes of water. **Being present as traces, removal of these ultratrace contaminants from wastewater is challenging. Adsorption of HMs onto raw (RPP) and burnt (BPP) potato peels (PP) is presented in the current treatise.** Both adsorbents (RPP and BPP) proved to be **efficient in removing Cd(II), Co(II), Cu(II), Fe(II), La(III), Ni(II), and Pb(II) from aqueous solutions.** BPP was a more efficient adsorbent compared to RPP.[\[Paper\]](https://www.hindawi.com/journals/jchem/2019/4926240/)
* Therefore, this study investigated whether **inexpensive humic substances (HS) from sewage sludge compost could effectively remove copper (Cu) and cadmium (Cd) from highly contaminated sandy clay loam (S1) and clay (S2).** [\[Art. #ARTNUM\]](#article-96093-281661659)
* **Many types of lignocellulosic biomass show effective binding of toxic heavy metals from industrial and environmental effluents.** Raw material for biosorption is typically low-cost and easily available, including agricultural waste or forest residues such as sawdust, bark, or needles. **This review concentrates on the accumulation of heavy metals by lignocellulosic biosorbents.** **Thus far, biosorption has not been economically feasible on a large scale and needs further development for profitability.** [\[Art. #ARTNUM\]](#article-96093-2920469717)
* Coconut shell, orange peel, rice husk, peanut husk, sawdust, fruit waste, rice husk (with silica), neem bark, black gram, waste tea; Turkish coffee, walnut shell and vinegar treated egg shells as adsorbents to remove heavy metals from wastewater. [ \[Art. #ARTNUM\] ;](#article-96093-2181530184)[ \[Art. #ARTNUM\] ; ](#article-96093-2074214500)[\[Art. #ARTNUM\]; ](#article-96093-2621005454) [\[Art. #ARTNUM\] ;](#article-96093-2482743097) [\[Art. #ARTNUM\]](#article-96093-2733512159)
* **Bagasse, a waste material from sugarcane has been studied as a biosorbent for removing heavy metals, Pb 2+ and Cu 2+ , in a continuous system using a packed bed column.** This study was undertaken to determine the influence of varying the bed height and flow rate on the breakthrough and saturation time. Moreover, lead ions are adsorbed more efficiently with an adsorption capacity of 4.54 mg/g compared to copper ions with 3.98 mg/g at the most feasible parameters having a flow rate of 100 mL/min and a bed height of 30 cm[ \[Art. #ARTNUM\]](#article-96093-1023130721)
* Zouboulis et al. (2002) proposed a process of biosorptive floatation for the removal of heavy metal ions (i.e., nickel, copper, and zinc ions) from aqueous solutions using grape stalks, a by-product of the winery industry. In pilot-scale experiments, two feed solutions containing different metal ion concentrations (low and high level) were contacted in counter-current mode with a biomass. This configuration allowed improvement of the performance of the biosorbent. Floatation separation experiments were conducted in 10-L columns. The removal of all tested metal ions was found to be satisfactory. The regenerated biomass was used in the second cycle. [\[Paper\]](https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3696181/#CR151)
**Nutrients:**
* The results reveal that the potential of **wheat straw**, a waste material, can be used as a low-cost sorbent for **removing ammonia nitrogen**.[ \[Art. #ARTNUM\]](#article-96093-2355542055)
* **Sulfide** is an unwanted anion present in tannery effluents. In this study, a raw material namely **rice husk** has been used to check its performance to remove sulfide ions from water in batch adsorption experiments. Rice husk was further pretreated with calcium chloride, zinc chloride and organic solvents to check any change in uptake capacity of the adsorbent. The results argue that rice husk could be a useful material to treat sulfide-containing wastewaters.[ \[Art. #ARTNUM\]](#article-96093-2087777554)
* Therefore, the following paper makes an effort towards putting forth a biological alternative for the **removal of chlorides from wastewater**. The present paper studies the suitability of **Parthenium sp.** as a sorbent for chloride removal. Further, variations in the efficiency of biosorption with respect to different pH, concentration and time were studied. The paper concluded that Parthenium sps. dried biomass is capable of achieving upto 40% reduction in the chloride content at Lab scale.[\[Paper\]](https://www.environmentaljournal.org/1-4/ujert-1-4-4.pdf)
| 1.2.1 | Organic waste materials |
|---|---|
| Adsorption of Heavy Metal (Cd 2+ , Cr 6+ and Pb 2+ ) from Synthetic Waste Water by Rice husk Adsorbent | |
| Industrial waste constitutes the major source of various kinds of metal pollution in natural water. There are at least 20 metals which cannot be degraded or destroyed. The important toxic metals are Cd2+, Cr6+ and Pb2+. There are numerous methods currently employed to remove and recover the metals from our environment and many physicochemical methods have been proposed for their removal from wastewater. Adsorption is one of the alternatives for such cases and is an effective purification and separation technique used in industry especially in water and wastewater treatments. Cost is an important parameter for comparing the adsorbent materials. Therefore, there is increasing research interest in using alternative low-cost adsorbents. The use of rice husk as the low-cost adsorbents was investigated as a replacement for current costly methods of removing heavy metal ions from aqueous solutions. The experiment results showed that maximum removal of Cadmium ion by rice husk adsorbent is 92%, Chromium ion is 83% and Lead ion are 93% at optimum condition. Keyword: Heavy Metal, Aqueous Solution, Rice husk, Adsorption. | |
| 12/01/2013 00:00:00 | |
| Link to Article | |
| 1.2.2 | Organic waste materials |
| Agricultural and Forestry Wastes Material as Potential Adsorbent for Heavy Metal Ions from Aqueous Solutions:a Review | |
| Agricultural and forestry wastes as bioadsorbents have been aroused great attentions due to its advantages such as low cost,easy to cross-linking reactive adsorption groups and it can be efficiently and quickly remove heavy metal ions in wastewater. Some of the treated adsorbents including sawdust,rice husks,peanut shell,straw,bark and bagasse show good adsorption capacities for Pb,Cr,Cd and Cu,with biosorption capacity from 50% to 100%. Chemically modified agricultural and forestry wastes exhibit higher adsorption capacities than unmodified forms. The mechanisms of biosorption process are not well understood,but it may be related to the process of physisorpion,chemisorption,surface adsorption,complexation,ion exchange and diffusion. Agricultural waste material being highly efficient,low cost and renewable source of biomass can be exploited for heavy metal remediation to enhance their applicability at industrial scale. | |
| 01/01/2014 00:00:00 | |
| Link to Article | |
| 1.2.3 | Organic waste materials |
| An overview of fruit waste as sustainable adsorbent for heavy metal removal | |
| Biosorption is an environmental friendly method for metal removal as it can be used as a cost effective and efficient technique for heavy metal removal. A lot of biomass can be choosed as biosorbent such as waste material from food processing and agriculture.ent. This paper will review the potential used of local fruit rind as biosorbent for heavy metal removal in wastewater. Heavy metals have been in various industries and resulted to a toxic condition in aquatic ecosystem. Therefore, various techniques have been employed for the treatment of metal-bearing industrial wastewaters including biological treatment through biosorption. Biosorption offers the advantages of low cost, good efficiency and production of sludge with high metal content is possible to avoid by the existence of metal recovery method from metal loaded biosorbent. The successful application of local fruit waste in treating wastewater containing heavy metals requires a deeper understanding of how biosorbent material proceeds. | |
| 08/01/2013 00:00:00 | |
| Link to Article | |
| 1.2.4 | Organic waste materials |
| Applications of the Biosorption Process for Nickel Removal from Aqueous Solutions - A Review | |
| Wastewaters and contaminants released to the aqueous environment increase due to developing industrialization and technology. These wastewaters should be treated before being discharged to water bodies. Also, reusable materials in wastewaters must be recovered by appropriate techniques. Discharge limits required by the authorities become more stringent with updated legislations. Nickel ions can be reusable by recovering it after the biosorption process. So, this will prevent the loss of raw materials in industries and it also affects the economy in a positive way. Conventional heavy metal removal processes may be costly and inadequate to meet the desired discharge limits and they exhibit low efficiencies. Eco-friendly and economical treatment technologies gain great importance in the removal and recovery of nickel from wastewaters. In this study, biosorption which is the subject of numerous studies and one of the heavy metal removal methods will be investigated, and nickel removal by this technique and th... | |
| 06/03/2017 00:00:00 | |
| Link to Article | |
| 1.2.5 | Organic waste materials |
| Biomass-derived biosorbents for metal ions sequestration: Adsorbent modification and activation methods and adsorbent regeneration | |
| Abstract Heavy metals released from industrial activities pose a significant threat to the environment and public health due to their reported toxicity even at trace levels. Although there are several available methods to treat or remove heavy metals from water and wastewater, the research focuses on development of technological solutions which sound environmental friendly and economically feasible, able to reduce the costs and maximize the efficiency. In this framework, the biosorption process, which uses cheap and non-pollutant materials, may be considered as an alternative, viable and promising, technology for heavy metal and metalloid ions sequestration and ultimately removal technology in the waste water treatment. However, there is as yet little data on full-scale applications for the design and testing of adsorption units using single biosorbents and their combinations to sequester heavy metal ions from multi-metal systems. Immediate research and development is hence earnestly required in this specific direction to further make progress this blooming technology and widen its scope of application to real situations needing heavy metal pollution remediation. This review provides a comprehensive appraisal of the equilibrium modeling of a number of biosorption processes as well as the structural, chemical and morphological modifications and activation of biosorbents. Further the relative merits of the methods used to recover sequestered heavy metal ions and regenerate biosorbents through desorption routes and their future applications are discussed. | |
| 03/01/2014 00:00:00 | |
| Link to Article | |
| 1.2.6 | Organic waste materials |
| Biosorption of cadmium by green coconut shell powder | |
| Abstract The effective removal of heavy metals from aqueous wastes is among the most important issues for many industrialized countries. The traditional treatment methods used to remove heavy metals from wastewaters have certain disadvantages such as incomplete metal removal, high reagent and energy requirements, generation of toxic sludge or other waste products that require disposal. The search for alternative and innovate treatment techniques has focused attention on the use of biological materials for metal removal and recovery technologies. Biosorption has gained important credibility during recent years because of its good performance and low cost. In the present study, the biosorption capacity of powder from coconut shell was studied for cadmium. The adsorption capacity of biomass was investigated by batch experiments. The influence of metal ion concentration and pH were evaluated and the results were fitted using adsorption isotherm models. The kinetic of cadmium biosorption was also investigated. | |
| 04/01/2006 00:00:00 | |
| Link to Article | |
| 1.2.7 | Organic waste materials |
| Biosorption of Few Heavy Metal Ions Using Agricultural Wastes | |
| Since a few years a lot of interest has been shown in monitoring environmental pollution caused by heavy metals. Many methods such as precipitation, electroplating, evaporation, ion exchange etc. have been employed in the treatment of waste water, but have not proven to be much advantageous due to greater sludge production, higher reagent requirement etc. Biosorption which can be defined as the selective sequestering of metal soluble species, resulting in the immobilization of the metals is a striking technology for retaining heavy metals from dilute solutions with high efficiency. Several prior studies and research in environmental biotechnology have shown that many biosorbents occurring in the environment have the capacity to remove heavy metals from solutions. This paper presents the potential and result of studies carried out on economically cheaper natural materials like agricultural wastes such as peanut shells and banana peels as biological adsorbent for the removal of toxic heavy metal ions from waste water. The different metal ions studied were lead, copper, zinc and cadmium. The biosorption of the above metals was studied by various techniques such as Atomic Absorption Spectrophotometry, X-ray Difftaction and Scanning Electron Microscopy. Using peanut shells, adsorption of metal ions shown was in the order of lead > zinc > copper > cadmium, whereas using banana peels adsorption was in the order of cadmium > copper > lead > zinc. X-ray Difftaction results showed the presence of zinc, copper, mercury whereas the images obtained from Scanning Electron Microscope showed metal adsorption on the surface clearly at a magnification power of 500 µm and 200 µm. | |
| 01/23/2014 00:00:00 | |
| Link to Article | |
| 1.2.8 | Organic waste materials |
| Biosorption of heavy metals by lignocellulosic biomass and chemical analysis | |
| Many types of lignocellulosic biomass show effective binding of toxic heavy metals from industrial and environmental effluents. Biosorption is an emerging option for conventional methods to remove heavy metals, some of them with even better efficiencies compared to conventional methods. Raw material for biosorption is typically low-cost and easily available, including agricultural waste or forest residues such as sawdust, bark, or needles. This review concentrates on the accumulation of heavy metals by lignocellulosic biosorbents. Thus far, biosorption has not been economically feasible on a large scale and needs further development for profitability. Industrial-scale wood-based biosorbent applications are especially still lacking. Moreover, due to legislative demands, there is an increasing need for accurate and reliable analytical methods for metal analysis of environmental and industrial effluents. In the future, biosorption processes are likely to become common, and the requirement for environmental monitoring will increase due to ever restricting regulations. This emphasizes not only the need for the development of feasible process solutions, but also a requirement for accurate analytical methods. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
| 1.2.9 | Organic waste materials |
| Biosorption of heavy metals by potassium hydrogen phosphate and sodium oxalate modified lignocellulosic waste | |
| Heavy metals are among the most toxic nuisances that pose a huge pressure on the environment. This in effect calls for for the development of a noble low cost and efficient technology for the removal of heavy metal from industrial effluents. In this particular research, lead (II) biosorption capacity of chemically modified lignocellulosic wastes (rice husk and sugarcane bagasse) has been studied. The two selected biosorbents are abundant and low cost biosorbents with promising potential to remove hazardous heavy metals from effluent streams. In the study, after executing rigorous investigation on the potential of several chemical modifiers, potassium hydrogen phosphate and sodium oxalate were found to be the best modifiers to improve the sorption capacity of rice husk and sugarcane bagasse. Besides, impact of particle size and pH has been studied. Characterization of the sorbent surfaces has been made before and after chemical modification and after sorption of heavy metals using furrier transform infra-red spectroscopy (FTIR). For the selected chemically modified sorbents of rice husk and sugarcane bagasse intensive study was performed on the sorption kinetics for varying metal and sorbent doses. | |
| 09/01/2011 00:00:00 | |
| Link to Article | |
| 1.2.10 | Organic waste materials |
| Biosorption of heavy metals-An overview | |
| During the last two decades, extensive attention has been paid on the management of environmental pollution causal by hazardous materials such as heavy metals. Decontamination of heavy metals in the soil and water around industrial plants has been a challenge for a long time. A number of methods have been developed for the removal of heavy metals from liquid wastes such as precipitation, evaporation, electroplating, ion exchange, membrane processes, etc. However, these methods have several disadvantages such as unpredictable metal ion removal, high reagent requirement, generation of toxic sludge, etc. Biosorption is a process, which represents a biotechnological innovation as well as a cost effective excellent tool for removing heavy metals from aqueous solutions. This article provides a selective overview of past achievements and present scenario of biosorption studies carried out on some promising natural biosorbents (algae, fungi, bacteria, yeast) and some waste materials which could serve as an economical means of treating effluents charged with toxic metallic ions. | |
| 09/13/2008 00:00:00 | |
| Link to Article | |
| 1.2.11 | Organic waste materials |
| Biosorption of Heavy Metals: Recent Trends and Challenges | |
| Water resources are of critical importance to both natural ecosystem and human developments. Increasing environmental pollution from industrial wastewater particularly in developing countries is of major concern. Heavy metal contamination exists in aqueous waste streams of many industries, such as metal-plating facilities, mining operations, tanneries, and pulp and paper. Some metals associated with these activities are cadmium, chromium, iron, nickel, lead, and mercury. Heavy metals are not biodegradable and tend to accumulate in living organisms causing diseases and disorders. Hence, there is a need to treat the wastewater containing toxic metals before they are discharged into the water bodies. Many physicochemical methods like coagulation, flocculation, ion exchange, membrane separation, and oxidation are available for the treatment of heavy metals. Major drawbacks of these methods are high sludge production, handling and disposal problems, high cost, technical constraints, etc. This necessitates cost-effective and environmentally sound techniques for treatment of wastewater containing heavy metals. During the beginning of twenty-first century, the increasing awareness and concern about the environment motivated research for new efficient technologies that would be capable of treating inexpensively wastewater polluted by toxic metals. This search brought biosorption to the foreground of scientific interest as a potential basis for the design of novel wastewater treatment processes. Several adsorbents are currently used which are by-products from agriculture and industries. Biosorption using low-cost adsorbents could be technically feasible and economically viable sustainable technology for the treatment of wastewater and industrial effluents. | |
| 01/01/2013 00:00:00 | |
| Link to Article | |
| 1.2.12 | Organic waste materials |
| BIOSORPTIVE NICKEL REMOVAL - AN INSIGHT INTO STUDIES AND RESEARCH | |
| Heavy metal from waste water can be removed by various physical, chemical and biological treatment methods. Nickel is one of the important heavy metal emitted from electroplating, battery, and catalyst industries. Biosorption of Nickel is effective and low cost treatment technique. It uses agricultural waste and there by reduces solid waste problem to a considerable extent. The method has unique advantage in its ability to adopt for different geographical areas according to availability of agricultural waste. The investigations show that the agricultural waste such as banana, mosambi peels, ground nut, coconut shells and rice husk has been used for Nickel removal with satisfactory to excellent results. By using these materials the percentage Nickel removal to the extent of 99 percent was observed by investigators. Also aspects such as isotherms, kinetics, modeling of this process are area of study for researchers because of the role of these aspects in optimum and effective removal of Nickel. Present review summarizes studies and research on biosorptive removal of Nickel from waste water. | |
| 02/25/2016 00:00:00 | |
| Link to Article | |
| 1.2.13 | Organic waste materials |
| Experimental Study on Heavy Metal Removal from Textile Industrial Wastewater Using Banana Peel and Activated Carbon from Coconut Shell as an Adsorbent | |
| The most important class of pollutants is the effluents (dyes) which are disposed directly to the river from the textile industries. This effluent contains several heavy metals like chromium and copper. Some of the heavy metals which are present in even smaller amount will cause a greater pollution. Disposal of the effluents into the water streams or precious water resource must be avoided. However there are various treatment methods before disposal, which will not be effective in the removal of heavy metals. Adsorption is recognized as an effective and economic method for low concentration heavy metal wastewater treatment. In the adsorption process numerous adsorbents are available. In this study, we used banana peel and activated carbon produced from coconut shell as a low cost adsorbent. A comparative study is done in order to make a comparison between the removal efficiency of chromium by these adsorbent. The dosage of adsorbents is about 10 grams, 15 grams, 20 grams which will create a situation of removing heavy metals. The adsorption process is done at the room temperature for about an hour for each adsorbent. The adsorption process is started with the initial concentration of 10 gram of each adsorbent and then gradually increased based on the removal percentage. At the end 25 gram of dosage is given beyond that which produces no change in the removal of heavy metals. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 1.2.14 | Organic waste materials |
| Experimental Study on Heavy Metal Removal from Textile Industrial Wastewater Using Banana Peel and Activated Carbon from Coconut Shell as an Adsorbent | |
| The most important class of pollutants is the effluents (dyes) which are disposed directly to the river from the textile industries. This effluent contains several heavy metals like chromium and copper. Some of the heavy metals which are present in even smaller amount will cause a greater pollution. Disposal of the effluents into the water streams or precious water resource must be avoided. However there are various treatment methods before disposal, which will not be effective in the removal of heavy metals. Adsorption is recognized as an effective and economic method for low concentration heavy metal wastewater treatment. In the adsorption process numerous adsorbents are available. In this study, we used banana peel and activated carbon produced from coconut shell as a low cost adsorbent. A comparative study is done in order to make a comparison between the removal efficiency of chromium by these adsorbent. The dosage of adsorbents is about 10 grams, 15 grams, 20 grams which will create a situation of removing heavy metals. The adsorption process is done at the room temperature for about an hour for each adsorbent. The adsorption process is started with the initial concentration of 10 gram of each adsorbent and then gradually increased based on the removal percentage. At the end 25 gram of dosage is given beyond that which produces no change in the removal of heavy metals. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 1.2.15 | Organic waste materials |
| Heavy Metal Removal from Wastewater Using Low Cost Adsorbents | |
| With the onset of industrialization mankind has witnessed various environmental issues in the society. This industrialization has not only brought development and prosperity but eventually disturbed the ecosystem. One of the impacts is visible, in form of water pollution. In the present study heavy metal contamination of water bodies has been discussed. Effluents from large number of industries viz., electroplating, leather, tannery, textile, pigment & dyes, paint, wood processing, petroleum refining, photographic film production etc., contains significant amount of heavy metals in their wastewater. The conventional methods of treatment of heavy metal contamination includes chemical precipitation, chemical oxidation, ion exchange, membrane separation, reverse osmosis, electro dialysis etc. These methods are costly, energy intensive and often associated with generation of toxic byproducts. Thus, the adsorption has been investigated as a cost effective method of removal of heavy metals from wastewater. In the present study various low cost adsorbent has been reviewed as an abatement of heavy metal pollution from wastewater. These adsorbent includes materials of natural origin like zeolites, clay, peat moss and chitin are found to be an effective agent for removal of toxic heavy metals like Pb, Cd, Zn, Cu, Ni, Hg, Cr etc. Apart from these various agricultural wastes like rice husk, neem bark, black gram, waste tea; Turkish coffee, walnut shell etc. were also established as a potent adsorbent for heavy metal removal. Beside that low cost industrial by products like fly ash, blast furnace sludge, waste slurry, lignin, iron (III) hydroxide and red mud, coffee husks, Areca waste, tea factory waste, sugar beet pulp, battery industry waste, sea nodule residue and grape stalk wastes have been explored for their technical feasibility to remove toxic heavy metals from contaminated water. | |
| 01/01/2015 00:00:00 | |
| Link to Article | |
| 1.2.16 | Organic waste materials |
| Heavy Metal Uptake by Agro based Waste Materials | |
| Presence of heavy metals in the aquatic systems has become a serious problem. As a result, there has been a great deal of attention given to new technologies for removal of heavy metal ions from contaminated waters. Biosorption is one such emerging technology which utilized naturally occurring waste materials to sequester heavy metals from industrial wastewater. The aim of the present study was to utilize the locally available agricultural waste materials for heavy metal removal from industrial wastewater. The wastewater containing hexavalent chromium was treated with biomass prepared from corn stalks. It was fund that a time of one hour was sufficient for sorption to attain equilibrium. The equilibrium sorption capacity after one hour was 0.375 mg.g -1 . The optimum pH was (2-2.5) for chromium. Ion exchange was the major removal mechanism along with physical sorption and precipitation. The biosorption data was well fitted to Langmuir adsorption model. The kinetics of biosorption process was well described by the pseudo 2nd order kinetics model. It was concluded that adsorbent prepared from corn stalks can be utilized for the treatment of heavy metals in wastewater. | |
| 11/11/2013 00:00:00 | |
| Link to Article | |
| 1.2.17 | Organic waste materials |
| HEAVY METALS REMOVAL FROM FOOD WASTE WATER OF RAIPUR AREA USING BIOADSORBENTS | |
| A simple cost effective and eco-friendly method for the remediation of heavy metals from food wastewater has been investigated. A novel biomaterial, Oscimum Sanctum Linn (Tulsi) a medicinal plant, was used for the removal of heavy metals from food wastewater and the method was also applied for real sample analysis. The presence of metal ions in food wastewater is extremely undesirable, as they are toxic to both lower and higher organisms. Under certain environmental conditions, metals may accumulate to toxic levels and cause ecological damage of the important metals, mercury, lead, cadmium, Arsenic, and chromium (VI), regarded as toxic to certain extent, but their extensive usage and increasing levels in the environment are serious concerns. Several bioadsorbents have the ability to remove the heavy metals and thereby making water contaminant free. Therefore, the search for efficient, eco-friendly and cost effective remedies for waste water treatment has been initiated. Recently efforts have been made to use cheap and available agricultural wastes such as coconut shell, orange peel, rice husk, peanut husk and sawdust as adsorbents to remove heavy metals from wastewater. Biosorption can be effective technique for the treatment of heavy metal bearing waste water resulting from human and industrial activities. In the present study the biosorption of heavy metals using the tulsi leaves and parameters affecting the biosorption of heavy metals; such as time, pH, Dosage, rpm, mesh size have been investigated. The present study shows that 80% of biosorption of lead and 60% of cadmium was observed. | |
| 01/01/2015 00:00:00 | |
| Link to Article | |
| 1.2.18 | Organic waste materials |
| Humic substances from sewage sludge compost as washing agent effectively remove Cu and Cd from soil | |
| Although commercially available biosurfactants are environmentally friendly and effectively remove heavy metals from soil, they are costly. Therefore, this study investigated whether inexpensive humic substances (HS) from sewage sludge compost could effectively remove copper (Cu) and cadmium (Cd) from highly contaminated sandy clay loam (S1) and clay (S2). The optimum HS concentration and pH were determined, as well process kinetics. Under optimum conditions, a single washing removed 80.7% of Cu and 69.1% of Cd from S1, and 53.2% and 36.5%, respectively, from S2. Triple washing increased removal from S1 to almost 100% for both metals, and to 83.2% of Cu and 88.9% of Cd from S2. Triple washing lowered the potential ecological risk (Eri) of the soils, especially the risk from Cd. HS substances show potential for treating soils highly contaminated with heavy metals, and HS from other sources should be tested with these and other contaminants. | |
| 10/01/2015 00:00:00 | |
| Link to Article | |
| 1.2.19 | Organic waste materials |
| Local fruit waste as a potential biosorbent for wastewater containing heavy metals: An overview | |
| Biosorption can be used as a cost effective and efficient technique for the removal of toxic heavy metal from wastewater. Waste material from industries such as food processing and agriculture may act as potential biosorbent. This paper highlighted the potential used of local fruit waste as biosorbent for heavy metal removal in wastewater. According to Malaysian regulation, the discharge of the effluents into the receiving environment should follow acceptable level. Therefore, various techniques have been employed for the treatment of metal-bearing industrial wastewaters including biological treatment through biosorption. Biosorption offers the advantages of low cost, good efficiency and production of sludge with high metal content is possible to avoid by the existence of metal recovery method from metal loaded biosorbent. The successful application of local fruit waste in treating wastewater containing heavy metals requires a deeper understanding of how biosorbent material proceeds. An overview of research focusing on biosorbent of heavy metal using local fruit waste will be presented. | |
| 09/01/2012 00:00:00 | |
| Link to Article | |
| 1.2.20 | Organic waste materials |
| Low-cost activated carbon for adsorption and heterogeneous ozonation of phenolic wastewater treatment | |
| This work is aimed at elaborating an innovative material from palm tree waste that can be used in industrial applications for adsorption and catalytic oxidation. This low-cost activated carbon, elaborated from Borassus palm tree waste (bpAC) showed textural and chemical properties comparable with common activated carbon. Moreover, it demonstrated interesting behaviour when it was coupled with ozone to remove a phenolic compound, 2,4-dimethylphenol (2,4-DMP). This refractory model molecule was removed two times faster in the presence of bpAC and was achieved in only 7 min. The total organic carbon (TOC) removal by only adsorption on bpAC was satisfactory with a value of 93.8% after 8 h. Nevertheless, the most interesting result concerned the TOC removal during catalytic ozonation which increased from 26% (single ozonation, i.e., without bpAC) to 91% in the presence of bpAC. The addition of a radical scavenger (tert-butanol) showed that hydroxyl radicals were involved during ozonation with bpAC. Moreover, a kinetics study highlighted that both radical and molecular mechanisms were acting in heterogeneous reaction. All the results were finally validated by treating real wastewater spiked with 2,4-DMP, confirming the ability of this bpAC to enhance the treatment of phenolic wastewaters. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
| 1.2.21 | Organic waste materials |
| Olive husk: an alternative sorbent for removing heavy metals from aqueous streams. | |
| Sorption properties of olive husk were investigated under equilibrium (batch tests) and dynamic (column tests) conditions in order to assess the possibility of using such a waste material for removing heavy metals from aqueous streams. Husk samples were contacted, at 25°C, with aqueous solutions of nitric salts of Pb, Cd, Cu, and Zn. Sorption isotherms obtained from equilibrium data were fitted and interpreted by the Freundlich model. Metals-saturated husk samples resulting from column tests were air-dried and incinerated to simulate combustion in order to assess the fate of sorbed metals. The results demonstrated that, under both equilibrium and dynamic conditions, metal sorption capacity of the husk was in the sequence Pb>Cd>Cu>Zn. For all the metals, calculated Freundlich constants decreased by increasing initial metal concentration or decreasing solution pH. In dynamic tests, a significant reduction of sorption capacity was recorded (except for copper) when a metal was fed simultaneously to the others: Pb (77%); Cd (93%); Zn (68%). Combustion tests carried out on metals-saturated husk samples showed that the average losses of lead and cadmium, as volatile species, were always three to four times greater than the losses of copper and zinc, in both single-metal- and multimetal-saturated samples. | |
| 01/01/2003 00:00:00 | |
| Link to Article | |
| 1.2.22 | Organic waste materials |
| Packed bed biosorption of lead and copper ions using sugarcane bagasse | |
| Bagasse, a waste material from sugarcane has been studied as a biosorbent for removing heavy metals, Pb 2+ and Cu 2+ , in a continuous system using a packed bed column. This study was undertaken to determine the influence of varying the bed height and flow rate on the breakthrough and saturation time. Thomas, Adams-Bohart and Yoon-Nelson models were used to assess the effects of varying parameters and both Thomas and Yoon-Nelson models were found to be satisfactory to describe the column data obtained in the experiment. Moreover, lead ions are adsorbed more efficiently with an adsorption capacity of 4.54 mg/g compared to copper ions with 3.98 mg/g at the most feasible parameters having a flow rate of 100 mL/min and a bed height of 30 cm | |
| 11/29/2016 00:00:00 | |
| Link to Article | |
| 1.2.23 | Organic waste materials |
| Removal of ammonium ions from wastewater A short review in development of efficient methods | |
| ABS TRACT: Ammonium ions wastewater pollution has become one of the most serious environmental problems today. The treatment of ammonium ions is a special concern due to their recalcitrance and persistence in the environment. In recent years, various methods for ammonium ion removal from wastewater have been extensively studied. This paper reviews the current methods that have been used to treat ammonium ion wastewater and evaluates these techniques. These technologies include ion exchange, adsorption, biosorption, wet air oxidation, biofiltration, diffused aeration, nitrification and denitrification methods. About 75 published studies (1979-2015) are reviewed in this paper. It is evident from the literature survey articles that ion exchange, adsorption and biological technology are the most frequently studied for the treatment of ammonium ion wastewater. | |
| 04/01/2015 00:00:00 | |
| Link to Article | |
| 1.2.24 | Organic waste materials |
| Removal of Heavy Metal from Industrial Wastewater Using Ultrasonic Assisted By Tea Waste As Adsorbent | |
| Wastewater from industry can lead to water pollution if untreated, especially due to its high concentration of heavy metals. Heavy metals are considered extremely harmful because they can cause illnesses, disorder and diseases to human. Therefore, industrial wastewater containing heavy metal should be treated before discharge to the water stream but its treatment is very costly. There are several techniques to remove heavy metals from wastewater such as biosorption, filtration and adsorption of heavy metal but there is some limitation such as long treatment time. This research is about the efficiency of combination method between ultrasonic and adsorption process to remove zinc, Zn and nickel, Ni from fertilizer factory wastewater. The parameters analyzed in this research are amounts of adsorbent in solutions from 0.5 g to 2.9 g of tea waste, different ultrasonic temperature from 40° C to 80° C and different sonication time from 5 minute to 29 minutes. After several experiment and analysis of results, it is found that the optimum condition to remove Zn and Ni from 100 ml wastewater is at 24 minute sonication time and 75°C ultrasonic temperature for 2.5 g amount of adsorbent which can remove about 79% of zinc and 71% of nickel. According to the result, the method of ultrasonic assisted by adsorption process to remove heavy metal from industrial wastewater can be use effectively because it can reduce energy, time and cost of treatment. | |
| 12/01/2010 00:00:00 | |
| Link to Article | |
| 1.2.25 | Organic waste materials |
| Removal of Heavy Metals from Industrial Wastewater Using Rice Husks | |
| Heavy metals are widely used in textile industries and significant losses occur during the manufacture and processing of textiles, and these lost heavy metals are discharged in the effluent. Adsorption of heavy metals is a new technology for treatment of wastewater containing different types of selected heavy metals. In this study, adsorbents Carbonized Rice Husk (CRH) and Activated Rice Husk (ARH) made out of rice husks, available as agriculture waste, are investigated as viable materials for treatment of Pb, Cd, Cu, and Zn containing industrial wastewater at controlled pH. The results obtained from the batch experiments revealed a relative ability of the rice husk in removing some heavy metals at pH 7. One hand one, the CRH adsorption capacity decreases in the order of Cu > Pb > Zn > Cd in batch adsorption whereas during Rapid Small Scale Column Tests the adsorption capacity decrease as follow Cu> Zn> Pb> Cd. On the other hand, ARH adsorption capacity performance is similar to CRH. However, during Rapid Small Scale Column Tests the adsorption capacity decreases in the order Zn>Cu>Pb>Cd. The kinetic removal in batch experiment shows that the net uptake of Pb, Cd, Cu, Zn was 54.3%, 8.24%, 51.4% and 56.7%, respectively whereas using CRH, while it varied as 74.04%, 43.4%, 70.08% and 77.2% for the same dosages of ARH. Therefore, it is concluded that as regards to CRH, ARH demonstrated higher potential to remove relatively all selected heavy metals. | |
| 11/16/2011 00:00:00 | |
| Link to Article | |
| 1.2.26 | Organic waste materials |
| Removal of heavy metals from water sources in the developing world using low-cost materials: A review | |
| Abstract Heavy metal contamination is a growing concern in the developing world. Inadequate water and wastewater treatment, coupled with increased industrial activity, have led to increased heavy metal contamination in rivers, lakes, and other water sources in developing countries. However, common methods for removing heavy metals from water sources, including membrane filtration, activated carbon adsorption, and electrocoagulation, are not feasible for developing countries. As a result, a significant amount of research has been conducted on low-cost adsorbents to evaluate their ability to remove heavy metals. In this review article, we summarize the current state of research on the removal of heavy metals with an emphasis on low-cost adsorbents that are feasible in the context of the developing world. This review evaluates the use of adsorbents from four major categories: agricultural waste; naturally-occurring soil and mineral deposits; aquatic and terrestrial biomass; and other locally-available waste materials. Along with a summary of the use of these adsorbents in the removal of heavy metals, this article provides a summary of the influence of various water-quality parameters on heavy metals and these adsorbents. The proposed adsorption mechanisms for heavy metal removal are also discussed. | |
| 05/01/2019 00:00:00 | |
| Link to Article | |
| 1.2.27 | Organic waste materials |
| Removal of Nickel (II) and Cobalt (II) from Wastewater Using Vinegar-Treated Eggshell Waste Biomass | |
| The use of waste materials as low-cost adsorbents is attractive due to their contribution in the reduction of costs for waste disposal, therefore contributing to environmental protection and most importantly, offers an attractive potential alternative to their conventional methods of removal of toxic ions from wastewater. Eggshells are naturally occurring and an abundant biomass that has proven to offer an economic solution for toxic ions removal. The eggshell biomass was treated with acetic acid (vinegar). Nickel (II) and Cobalt (II) ions were selected as model ions to demonstrate the potential of eggshell waste in removing excess toxic heavy metal ions from wastewater. All the experiments were carried out in batch process with laboratory prepared samples. Multivariate optimization method was used to identify factors affecting adsorption. These factors included metal ion concentration, pH, contact time and biomass dosage on removal of nickel and cobalt from wastewater effluent was investigated. Two-level fraction factorial and central composite design were used for optimization methods. Fourier Transform Infrared Spectroscopy, Raman Spectroscopy, and Scanning Electron Microscopy coupled with Energy-dispersive X-ray spectroscopy were used to study physical properties of the waste material. The percentage removal of Nickel (II) and Cobalt (II) was 78.70 ± 1.02 and 76.53 ± 1.21 respectively. Vinegar-treated eggshells were proposed as eco-friendly, cheap, easily available and an efficient method for removal of heavy metals from the environment. | |
| 01/01/2017 00:00:00 | |
| Link to Article | |
| 1.2.28 | Organic waste materials |
| Removal of sulfide ions from water using rice husk | |
| Sulfide is an unwanted anion present in tannery effluents. In this study, a raw material namely rice husk has been used to check its performance to remove sulfide ions from water in batch adsorption experiments. The effects of various physical parameters such as contact time, pH, shaking speed and temperature have been investigated to optimize the conditions for maximum adsorption efficiency. Rice husk was further pretreated with calcium chloride, zinc chloride and organic solvents to check any change in uptake capacity of the adsorbent. Langmuir, Freundlich and Temkin isotherms were used to explain the nature and mechanism of adsorption. The results argue that rice husk could be a useful material to treat sulfide-containing wastewaters. | |
| 03/04/2015 00:00:00 | |
| Link to Article | |
| 1.2.29 | Organic waste materials |
| Removal of toxic heavy metals: natural products َas biosorbents | |
| Background: Industrial effluents loaded with heavy metals are a cause of seirous hazards to human and other forms of life. However, conventional methods such as precipitation, ion exchange, electrodialysis, etc. used for the removal of heavy metals from wastewater, are often cost prohibitive having inadequate efficiencies at low metal ion concentration. Biosorption can be considered as an alternative technology which has been proved as more efficient and economical for the removal of heavy metals from the industrial wastewater. This study aimed to review the use of some natural biosorbents for removing toxic heavy metals from water and wastewater. Materials and Methods: In this research different biosorbents were used. Biosorbents were ground and sieved into size 250-500 µm. The samples were analyzed using various methods for the determination of metal ions concentration. Results: The biosorption of metals such as copper, zinc, lead, iron and cadmium by coffee beans showed that all metals were adsorbed at low pH 3-5. The absorption capacity of egg shell (160 mg/g) for Cr (III) was reported. Conclusion: The recent survey shows the potential use of natural products such as tea leaves, tea waste, rice husk, orange peel, coffee seeds, wheat stem, egg sell, etc., as biosorbents for removing heavy metals from aqueous solutions. Mathematical modelings are also helpful for biosorption process optimization. | |
| 01/01/2013 00:00:00 | |
| Link to Article | |
| 1.2.30 | Organic waste materials |
| Rice husk silica derived nanomaterials for sustainable applications | |
| Rice husk (RH) is an abundant and sustainable waste biomass. Silica-rich RH can be converted to biofuels (e.g., bio-oil, vapors) and biochars simultaneously via thermochemical processes such as pyrolysis, gasification. Bio-oil can be further upgraded into renewable biofuels (e.g., biodiesel) by using the RH-derived catalysts. Meanwhile, vapors from organic matters decomposition can be converted to value-added syngas for energy purpose or chemical synthesis by using the RH silica materials, which are used for gas cleaning or catalytic reforming. In general, the applications of RH-derived biochars mainly include soil remediation, pollutants removal, silicon battery materials, and so on. This paper reviewed recent progresses in the syntheses of RH silica materials and their sustainable applications, especially in energy and environment functional materials. As for the environmental issues, the RH-silica materials can remove heavy metals and organic contaminants in soil amendment, wastewater treatment, and gas purification by means of adsorption, catalysis and integrated processes. In summary, biomass with high content of silica can become a potential resource of low cost precursors for the production of high value-added silica/silicon materials for practical applications. | |
| 12/01/2017 00:00:00 | |
| Link to Article | |
| 1.2.31 | Organic waste materials |
| Studies on Separation of Heavy Metals from Aqueous Solutions Using Biosorbents | |
| Man is blessed with an abundance of nature. But in the name of development, the nature is being continuously destroyed by man. As a result, nature is polluted beyond the measure because of an indiscriminate release of heavy metals into the environment. Industrialization and urbanization pose a significant problem to the biosphere. Heavy metal ions do not degrade but harm human body, flora, fauna, and the environment. Biosorption is one of the most effective techniques to remove heavy metals from industrial effluents. The low cost-natural products and waste substances are found to be very effective in the removal of heavy metals from industrial wastewaters. The objective of the present study is to developinexpensive, eco-friendly and useful metal ion adsorbents that are available in large quantity. As an alternative to existing commercial adsorbents for the removal of different heavy metal ions like chromium, lead and cadmium from synthetic aqueous solutions. In the present work different low cost natural adsorbents such as coconut shell, tamarindus indica, Mangifera indica, Moringa oleifera and waste products such as pineapple peel and soap nut seeds (The Drupe of sapindus plants, containing saponins which are natural surfactants) were used to determine adsorption efficiency in removing chromium, lead and cadmium. All these adsorbents were used without any pre-treatment. The influence of contact time,pH, temperature, adsorbent dose and initial metal ion concentration on the selectivity and sensitivity of the removal process was investigated. The removal of these metal ions from aqueous solutions/industrial effluents was studied using the batch method. It was observed that the rate of adsorption increased with the increase in adsorbent dose. The maximum time for higher adsorption rates was found between 120 to 150 min. The optimum pH for the separation observed was 2. Finally, based on the results obtained, the researcher would like to conclude that the use of low-cost adsorbents for metal ion removal which is feasible and eco-friendly. The results are presented and tabulated. | |
| 08/10/2018 00:00:00 | |
| Link to Article | |
| 1.2.32 | Organic waste materials |
| Study on the absorption of ammonia nitrogen by using carbonized wheat straw | |
| The present article is aimed at the study of the sewage treatment efficiency by using carbonized wheat straw,For this purpose,first of all,the article tested three important factors that may affect the absorption process,including the choice of the carbonization temperature,adsorption temperature,and the pH value.Secondly,we have worked out all the kinetic data respectively by means of pseudo-first-order equation,pseudo-second-order equation,Elovich equation and the intra-particle diffusion model.Thirdly,we have analyzed the equilibrium isotherms by using the Langmuir and the Freundlich.And,finally,calculation was done to race the free energy changes ΔG,the enthalpy changes ΔH and enthalpy changes ΔS via the thermodynamics equation.The experimental results indicate that the optimal temperature for direct carbonization proves to be 300 ℃. Within the scope of the pH value,the optimal pH value for the ammonia nitrogen adsorption tends to be 9,whereas the carbonized wheat straw can adsorb different mass concentration(ρ=30 mg/L,50 mg/L,100 mg/L) of the ammonia nitrogen,which may follow the pseudo-second-order kinetics and the adsorption constant k2 (0.681 8 g/(mg·min),0.747 4 g/(mg·min),1.025 g/(mg·min)),but the intra-particle diffusion would not be the main rate-controlling step for the ammonia nitrogen adsorption onto the carbonized wheat straw.At the same time,the result of the given study also indicates that the higher the temperature,the better the absorption would be.The adsorption temperature of ammonia nitrogen on the adsorbent,the carbonized wheat straw,is 30 ℃.Therefore,all the above methods prove to be helpful for enhancing the capacity to remove ammonia nitrogen from the sewage to a great extent.In addition,the equilibrium data tends to fit well with the model Freundlich at 15 ℃,25 ℃and 35 ℃ respectively.In addition,the enthalpy changes(ΔH) and the entropy changes(ΔS) are positive,while the free energy changes(ΔG) are negative.Thus,the thermodynamic study proves that the adsorption process is a spontaneously endothermic process,implying that ammonia nitrogen adsorption by carbonized wheat straw might be of physisorption by nature.The results reveal that the potential of wheat straw,a waste material,can be used as a low-cost sorbent for removing ammonia nitrogen. | |
| 01/01/2012 00:00:00 | |
| Link to Article | |
| 1.2.33 | Organic waste materials |
| The Efficiency of Cactus Leaves and Wood Charcoal as a Potential Low-Cost Adsorbent for Removal of Toxic Heavy Metals from Industrial Effluents | |
| Presence of toxic heavy metals in the environment is of great concern due to their persistence in nature and chronic adverse effects on human health and the environment. Present paper tries to evaluate the efficiency of cactus leaves ( Opuntia f. indica ) and activated carbon made from acacia etbiaca as an adsorbent for the removal of heavy metal pollutants such as cadmium, lead and chromium from water. Adsorption properties such as size, dose, initial concentration and time of contact for cadmium, lead and chromium were studied through batch method. Before removing the toxic heavy metals (Cd, Pb and Cr), the fresh unpeeled cactus leaves (adsorbent) and activated carbon were washed with distilled water to eliminate the turbidity and smell from fresh unpeeled cactus. To describe the equilibrium isotherms, the experimental data were analyzed by the Langmuir and Freundlich isotherm models. Thus, the Freundlich model gave the best correlation with the experimental data. Therefore, the findings indicated that the cactus and activated carbon made locally from acacia etbiaca were found to be effective and low-cost alternative adsorbents for the removal of toxic heavy metals from industrial effluents. The preparation method allowed the use of these materials by local industries for effective remediation of pollution by removing heavy metals from their effluents. Keywords : Cactus leaves; Acacia etbiaca ; Heavy metals; Adsorption, Industrial effluents; Water purification. | |
| 02/15/2019 00:00:00 | |
| Link to Article | |
1.3 Biosorption
Biosorption is sorption using (usually inactive) biomass. Numerous studies have been carried out with bacterial, fungal and algal biomass as biosorbents. Here the biomass does not actively take up the pollutants (as in [\[Bioleaching\]](#technology-95812)).
Selectivity is very dependent on the type of material and on the concentrations in the waste stream. It can be highly selective for only 1 contaminant, or be more general. Some pre-treatments, as well as engineering strategies exist to tailor this, which is a very active field of research. [\[Paper\]](https://www.researchgate.net/publication/262527665_New_Biosorbent_Materials_Selectivity_and_Bioengineering_Insights)
**Generally, the binding mechanisms that cause biosorption include ion exchange, micro-precipitation and electrostatic interactions.** [\[Art. #ARTNUM\]](#article-96076-2783282207)
The capacity of biomass to retain the metal ions from aqueous media (natural or residual) is manifesting by mechanisms such as: chelatization, initial solubilization by protons, formation of inorganic complexs, ionic exchange and dissolution of linking sublayers of metals by reduction reactions, the major contribution being of chelatization. This diversity of mechanisms, together with the interdependence between them is determined, in principal, by the compositional variety of biomass, which can retain the metal ions through functional groups of different type as: carboxyl, phosphate, hydroxyl, amino, thiol The ellution of metals from biosorbents is performed with alkaline solutions (Na2CO3), ethylene diamino tetraacetic acid or with dilluted solutions of mineral acids (HCl, HNO3, H2SO4). To the use of some cheap biomasses (sludges) and retaining of precious or rare metals (gold, silver, uranium) it is practiced the recovery of cations by biosorbent incineration. [\[Paper\]](https://www.researchgate.net/publication/267633071_Biosorption_-_current_bioprocess_for_wastewater_treatment)
**Algae:**
* **In conclusion, the presence of various functional groups, hydroxyl, carboxylic and amine groups, in all MA (marina algae) and FA (freshwater algae) samples had enabled the algae biomass to adsorb heavy metals of Cu, Pb, Cd and Zn from synthetic and industrial water.** Due to their bio-sorptive properties and fast adsorption capability, algae could be a potential method for cleaning up surface water or post-treatment of wastewater and minimise the cost of eutrophication.[ \[Art. #ARTNUM\]](#article-96076-2540464837)
* Biosorption method by microalgae is one of the newest methods which have the properties such as cost, selective adsorption, high processing rate and no sludge production. In this process in order to clean up wastewater by adsorption, the two algae Chlorella and Spirulina are optimal. In comparing these two algaes, Chlorella algaehas better ability to attract as well as more balanced with the absorption effect. [\[Art. #ARTNUM\]](#article-96076-2268465717)
* The biosorption capacity of microalgae is due to their high surface-to-volume ratio and high binding affinity. The mechanisms involved in biosorption include ion exchange, complexation, precipitation and physical adsorption. Functional sites on the cell wall of microalgae involved in biosorption include carboxyl, imidazole, sulfhydryl, amino, phosphate and sulphate moieties. [\[Art. #ARTNUM\]](#article-96076-2943002655)
**Bacteria & Fungi:**
* A variety of biomaterials are known to bind these pollutants, including bacteria, fungi, algae, and industrial and agricultural wastes. In this review, the biosorption abilities of bacterial and fungal biomass towards metal ions are emphasized. [\[Art. #ARTNUM\]](#article-96076-2185808385)
* In the mechanism of ion exchange, the metal ion within the wastewater is replaced by another similarly charged ion. Ion exchange is the dominant mechanism for the removal of Cu(II), Ni(II), Zn(II), Pb(II), and Cr(III) by Penicillium chrysogenum. The same mechanism is also involved in removing Cd(II) by Saccharomyces cerevisiae. The biosorption of Pb (II) and Cd(II) onto Amanita rubescens biomass was also mainly due to the ion-exchange between the hydrogen atoms of amine (-NH), hydroxyl (-OH) and carboxyl (-COOH) groups of the biomass and the metal ions. Chelation is another metal binding mechanism in biosorption where the metal ions bind with an organic molecule to form a ring structure. Different functional groups present in cells that take part in chelation are carboxyl, sulphydryl, amino, sulphate, phosphate, thioether and carbonyl groups. A chelation process is responsible for the biosorption of Pb(II) onto iron oxide nanoparticles immobilized Phanerochaete chrysosporium cells. The same mechanism took place in the removal of Cr (VI) using surface modified P. chrysosporium. **The use of microorganisms as adsorbents is efficient, cost-effective and safe for the removal of heavy metals from soils, sediments and water.** [\[Art. #ARTNUM\]](#article-96076-2783282207)
**Agricultural use of biomass+contaminants:**
* Zootechnical studies were performed on laying hens in order to investigate utilitarian properties of new biological feed supplements with microelements. **Macroalgae enriched with Mn(II), Zn(II), Cu(II), Co(II), and Cr(III) ions via biosorption process, confirmed that the bioavailability of microelements from biological feed additives was higher in comparison with traditionally used inorganic salts.** Hens, which were fed with enriched macroalgae, were heavier, laid larger eggs with thicker shells, which were characterized by more intense color of yolks. The eggs of hens fed with algal additives were biofortified with Cu, Cr, and Mn. [\[Paper\]](https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3696181/#CR151)
**Commercial:**
* The first pilot plant installations of biosorption technology appeared in the USA and Canada. In the 1990s, several commercial biosorbents have been proposed for the removal of heavy metal ions from industrial or mining wastewaters. Among them BIO–FIX, AMT–BIOCLAIM™, AlgaSORB™ are the most popular sorbents prepared by immobilization of specific biomaterials.
* US Bureau of Mines (Golden, CO, USA) proposed a new sorbent namely BIO–FIX beads for the heavy metal ions removal from industrial wastewaters, acid mine drainage (AMD) waters and ground waters. These sorbents incorporated a biomass of cyanobacteria (*Spirulina*), yeasts, algae or plants (*Lemna* sp., *Sphagnum* sp.), immobilized in polymeric (polysulphone, polyethylene, polypropylene) porous beads. This sorbent was used in packed bed and fluidized bed columns as well as in simple low-maintenance troughs system. Screening tests have shown that this sorbent is very efficient and useful in treatment of waters containing heavy metal ions in the range of micrograms per liter (initial concentration of around 50 mg L^−1^). In addition, long-term usage of BIO–FIX beads in repeated sorption–desorption cycles (with mineral acids as eluents) have shown that this sorbent is very effective and stable (over 9 % of sorption capacity after 200 cycles). Pilot–plant tests with three columns, each contained 284 L of beads (over 3.8 million liters of treated waters), confirmed a very good sorbent performance.
* Advanced Mineral Technologies, Inc. (AMT) has employed a new sorbent, AMT–BIOCLAIM™, obtained from industrial fermentation process (i.e., *Bacillus subtilis*). Granular biomass, called metal recovery agent, about 0.1 mm size, effectively removed heavy metal ions from wastewater (efficiency over 99 % especially for Ag, Cd, Cu, Pb, and Zn) and recovered precious metals (Au from gold cyanide solutions with uptake 394 mg g^−1^). Economic analysis indicated that the process is 50 % cheaper than chemical precipitation and about 28 % than ion exchange.
* An algal biosorbent AlgaSORB™, *Chlorella vulgaris* immobilized on silica gel polymer matrix, has been developed by Bio-Recovery System, Inc. (Las Cruces, USA) and this sorbent was employed to treat heavy metal ions from diluted solutions (1–100 mg g^−1^). This biological ion-exchange resin was able to bind both metallic cations and metallic oxoanions and could be competitive to commercial ion-exchange resins.
* B.V. SORBEX, Inc. (Montreal, Canada) started by popular biosorption researcher Bohumil Volesky offered a commercial sorbent, metal-binding biomass, BV–SORBEX™. Biosorbents family included powders and granules of size between 0.1 and 3 mm, consisting of algae (*S. natans*, *A. nodosum*, *H. opuntia*, *P. pamata*, *C. Crispus*, and *C. vulgaris*). Uptake of metal ions by this sorbent was independent on solution concentration and was able to remove metal ions from concentrated or diluted solutions with high efficiency (over 99 %).
* MetaGeneR and RAHCO Bio-Beads were two other commercial biosorbents which could be used as effective materials for removal of heavy metal ions from wastewaters (mainly electroplating and mining industry).[ ](https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3696181/#CR151)[\[Art. #ARTNUM\]](#article-96076-2311968619)
* **The process of biosorption has been recently commercialized and accepted by EPA (EPA/540/S5-90/005)**. [\[Paper\]](https://www.sciencedirect.com/science/article/pii/S0160412009002396#aep-section-id19)
Suppliers
| 1.3.1 | Biosorption |
|---|---|
| A comparative study of phosphorus removal using biopolymer from aerobic granular sludge: A factorial experimental evaluation | |
| Abstract This work presented an integrated approach to recover nutrients and biomaterials from wastewater, resulting in a phosphorus-enriched biomaterial with the potential for additional applications. The present investigation explored phosphorus removal from liquid samples using ALE recovered from aerobic granular sludge. The pH of the phosphorus solution, dosage of ALE beads, temperature and initial phosphorous concentration were factors tested through a factorial experimental design, with the results compared with commercial seaweed alginate. The ALE recovery from discarded aerobic sludge granules was 21.29 ± 1.57%. ALE beads demonstrated the potential to remove phosphorus (49.54 ± 2.23%) from liquid samples better than commercial seaweed alginate (36.78 ± 2.10%). The results from the factorial experiment indicated pH and dosage of ALE beads as the main parameters for phosphorus removal. Regeneration of ALE beads and the phosphorus recovery experiments showed the potential of using this biomaterial as a biodegradable phosphorus slow-release source. | |
| 11/01/2019 00:00:00 | |
| Link to Article | |
| 1.3.2 | Biosorption |
| Adsorption Of Heavy Metals Onto Wastewater Treatment Plant Sludge | |
| Heavy metals containing wastewater can cause serious environmental pollution problems for aquatic life. Adsorption is a well-established technique for pollutants removal and activated carbon is a widely used adsorbent material. However, use of activated carbon can be expensive due to the regeneration required and loses in the application processes. Biosorption is a recent technology used to remove heavy metal ions from aqueous solutions. In recent years investigators have studied inexpensive alternative materials for removal of heavy metal from wastewaters. Significant amount of waste sludge is produced in the industrial and municipal waste water treatment plant. Waste sludge disposal is one of the most important problems in the world. The waste activated sludge provides an excellent opportunity for removal of heavy metals by biosorption because of its availability and free use. Usage of the waste sludge as biosorbent was evaluated in this study. | |
| 07/07/2016 00:00:00 | |
| Link to Article | |
| 1.3.3 | Biosorption |
| Applications of the Biosorption Process for Nickel Removal from Aqueous Solutions - A Review | |
| Wastewaters and contaminants released to the aqueous environment increase due to developing industrialization and technology. These wastewaters should be treated before being discharged to water bodies. Also, reusable materials in wastewaters must be recovered by appropriate techniques. Discharge limits required by the authorities become more stringent with updated legislations. Nickel ions can be reusable by recovering it after the biosorption process. So, this will prevent the loss of raw materials in industries and it also affects the economy in a positive way. Conventional heavy metal removal processes may be costly and inadequate to meet the desired discharge limits and they exhibit low efficiencies. Eco-friendly and economical treatment technologies gain great importance in the removal and recovery of nickel from wastewaters. In this study, biosorption which is the subject of numerous studies and one of the heavy metal removal methods will be investigated, and nickel removal by this technique and th... | |
| 06/03/2017 00:00:00 | |
| Link to Article | |
| 1.3.4 | Biosorption |
| Bioremediation of Heavy Metal by Algae | |
| Instead of using mainly bacteria, it is also possible to use mainly algae to clean wastewater because many of the pollutant sources in wastewater are also food sources for algae. Nitrates and phosphates are common components of plant fertilizers for plants. Like plants, algae need large quantities of nitrates and phosphates to support their fast cell cycles. Certain heavy metals are also important for the normal functioning of algae. These include iron (for photosynthesis), and chromium (for metabolism). Because marine environments are normally scarce in these metals, some marine algae especially have developed efficient mechanisms to gather these heavy metals from the environment and take them up. These natural processes can also be used to remove certain heavy metals from the environment. The use of algae has several advantages over normal bacteria-based bioremediation processes. One major advantage in the removal of pollutants is that this is a process that under light conditions does not need oxygen. Instead, as pollutants are taken up and digested, oxygen is added while carbon dioxide is removed. Hence, phytoremediation could potentially be coupled with carbon sequestration. Additionally, because phytoremediation does not rely on fouling processes, odors are much less a problem. Microalgae, in particular, have been recognized as suitable vectors for detoxification and have emerged as a potential low-cost alternative to physicochemical treatments. Uptake of metals by living microalgae occurs in two steps: one takes place rapidly and is essentially independent of cell metabolism – “adsorption” onto the cell surface. The other one is lengthy and relies on cell metabolism – “absorption” or “intracellular uptake.” Nonviable cells have also been successfully used in metal removal from contaminated sites. Some of the technologies in heavy metal removals, such as High Rate Algal Ponds and Algal Turf Scrubber, have been justified for some practical application in China and abroad and limitations of these methods in large-scale still exist. As an innovative clean-up technology, it mainly depends on the biosorption and bioaccumulation abilities of algae, and the former is dominated in the whole process of bioremediation. Studies suggest that the constituents of algae cell wall such as alginate and fucoidan which have key functional groups are chiefly responsible for biosorption of heavy metal ions. | |
| 07/01/2012 00:00:00 | |
| Link to Article | |
| 1.3.5 | Biosorption |
| Biosorption of Heavy Metal by Algae Biomass in Surface Water | |
| Discharging wastewater containing heavy metals of Cu, Pb, Zn and Cd into water bodies can cause toxicity in plants and aquatic animals and some of them will be unable to survive except algae. Wastewater treatment method to remove heavy metal contaminants includes chemical precipitation, ion exchange, membrane, filtration, adsorption using activated carbon. However, these methods are either expensive or have other disadvantages such as high energy consumption and inefficiencies when existing heavy metals are at trace concentration. Biosorption using algae biomass can be an alternative method to eliminate heavy metals. The objective of the project is to investigate the capability of Marine Algae (MA) and Freshwater Algae (FA) bi-omass in adsorbing heavy metals of Cu, Pb, Zn and Cd from water medium using synthetic water and industrial water. MA and FA were obtained from the eastern coast of Pulau Ubin and local fish farm respectively. After being fully washed with deionised water, dried in a furnace for 105°C, they are grinded to pass 1 mm2 of siever. MA and FA were characterised using FTIR to determine their functional groups. An industrial water was collected from industrial discharge from metal fac-tories in northern side of Singapore. Effect of adsorption time, adsorbent concentra-tion, and pH were studied. The result showed that FA and MA had a higher capability in adsorbing a total metal of about 40 ppm level from an industrial water, or 4 times than synthetic water concentration, at the same adsorbent dosage of 50 mg. In con-clusion, the presence of various functional groups, hydroxyl, carboxylic and amine groups, in all MA and FA samples had enabled the algae biomass to adsorb heavy metals of Cu, Pb, Cd and Zn from synthetic and industrial water. Due to their bio-sorptive properties and fast adsorption capability, algae could be a potential method for cleaning up surface water or post-treatment of wastewater and minimise the cost of eutrophication. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 1.3.6 | Biosorption |
| Biosorption of Heavy Metal Pollution by Enterobacter agglomerans | |
| Biosorption is a new waste treatment technology that can eliminate toxic heavy metals. Biosorption can be considered as an environmentally friendly alternative technology to treat industrial liquid waste that is economically proper to use. One of them is biosorption that utilizes the microorganisms’ absorption ability, especially bacteria that can absorb heavy metals in waters, such as Enterobacter agglomerans . This research aimed to determine the ability of E. agglomerans in reducing heavy metals pollution in local river. The research employed the measurement of the effect of lead (Pb) to E. agglomerans growth using Optical Density (OD) at wavelength 600 nm. The colony numbers were calculated using a standard curve. While the ability of E. agglomerans to reduce heavy metals concentration in liquid media was measured using AAS with a wavelength of 240 nm. The results showed that lead affected the growth of E. agglomerans . The OD value has a negative relationship with the concentration level of Pb. The ODs were decreased from 2.867 to 1.242, using Pb level from 0 ppm to 20 ppm. Therefore, it proved that E. agglomerans could reduce heavy metals concentration in local river in Central Java Province. This research was the first report on E. agglomerans activity on heavy metal in contaminated water. This result can be used as a reference for industrial sites near the river to treat their wastewater before discharging it to the river body to preserve its water purity. | |
| 08/19/2019 00:00:00 | |
| Link to Article | |
| 1.3.7 | Biosorption |
| Biosorption of Heavy Metals and Dyes from Industrial Effluents by Microalgae | |
| Discharge of industrial effluents containing heavy metals and dyes is of concern as the pollutants may adversely affect the environment by contaminating surface- and groundwater resources. Heavy metals and dyes are very persistent and may pose a threat to various organisms and human health. Physicochemical methods such as chemical precipitation and adsorption are commonly used to remove heavy metals, while flocculation, flotation, membrane filtration and activated carbon are used to treat dye wastewater. However, these conventional technologies are costly and may not be fully effective in removing heavy metals and dyes. Biosorption refers to the ability of living or dead biomass to sequestrate pollutants such as heavy metals and dyes through passive binding. The biosorption capacity of microalgae is due to their high surface-to-volume ratio and high binding affinity. The mechanisms involved in biosorption include ion exchange, complexation, precipitation and physical adsorption. Functional sites on the cell wall of microalgae involved in biosorption include carboxyl, imidazole, sulfhydryl, amino, phosphate and sulphate moieties. Despite the extensive research in this area, there has been limited success in commercializing the technologies using algal biosorbents. Detailed economic and market analyses are required to assess the feasibility of the technologies. Integration of wastewater treatment and biofuel production with heavy metal and dye removal using biosorption process would be an attractive approach. Apart from treating the wastewater, the microalgae can be harvested for biofuel production, and the residual biomass can be used for biosorption of heavy metals and dyes. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
| 1.3.8 | Biosorption |
| Biosorption of heavy metals by lignocellulosic biomass and chemical analysis | |
| Many types of lignocellulosic biomass show effective binding of toxic heavy metals from industrial and environmental effluents. Biosorption is an emerging option for conventional methods to remove heavy metals, some of them with even better efficiencies compared to conventional methods. Raw material for biosorption is typically low-cost and easily available, including agricultural waste or forest residues such as sawdust, bark, or needles. This review concentrates on the accumulation of heavy metals by lignocellulosic biosorbents. Thus far, biosorption has not been economically feasible on a large scale and needs further development for profitability. Industrial-scale wood-based biosorbent applications are especially still lacking. Moreover, due to legislative demands, there is an increasing need for accurate and reliable analytical methods for metal analysis of environmental and industrial effluents. In the future, biosorption processes are likely to become common, and the requirement for environmental monitoring will increase due to ever restricting regulations. This emphasizes not only the need for the development of feasible process solutions, but also a requirement for accurate analytical methods. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
| 1.3.9 | Biosorption |
| Biosorption of heavy metals-An overview | |
| During the last two decades, extensive attention has been paid on the management of environmental pollution causal by hazardous materials such as heavy metals. Decontamination of heavy metals in the soil and water around industrial plants has been a challenge for a long time. A number of methods have been developed for the removal of heavy metals from liquid wastes such as precipitation, evaporation, electroplating, ion exchange, membrane processes, etc. However, these methods have several disadvantages such as unpredictable metal ion removal, high reagent requirement, generation of toxic sludge, etc. Biosorption is a process, which represents a biotechnological innovation as well as a cost effective excellent tool for removing heavy metals from aqueous solutions. This article provides a selective overview of past achievements and present scenario of biosorption studies carried out on some promising natural biosorbents (algae, fungi, bacteria, yeast) and some waste materials which could serve as an economical means of treating effluents charged with toxic metallic ions. | |
| 09/13/2008 00:00:00 | |
| Link to Article | |
| 1.3.10 | Biosorption |
| Biosorption, an efficient method for removing heavy metals from industrial effluents: A Review | |
| Abstract Common methods for removing heavy metals have numerous drawbacks, including low efficiency and high costs. In the biosorption of heavy metals, ions biosorbed on surfaces and active sites of biosorbents. In this paper, the relationship between the factors (pH, temperature, biosorbent dosage, retention time and Functional groups) and removal efficiency has been investigated. The purpose of this work is to introduce optimal conditions for biosorption reaction. Also, by introducing various types of biosorbents, expressed the advantages and method of preparation for each one. In various papers, not all biosorption isotherm models have been mentioned, there are described various types of biosorption isotherm, kinetics and thermodynamics models and important process data is set up for quick access to the tables. | |
| 02/01/2020 00:00:00 | |
| Link to Article | |
| 1.3.11 | Biosorption |
| Characteristics and function of macroalgae biosorption technology to metal ion | |
| Biosorption is a new technique which utilizes inexpensive living/dead organisms(fungi or algae) to adsorb heavy metals and is particularly useful for the removal of contaminants from industrial effluents. Compared with conventional methods such as ion exchange and precipitation with lime , the biosorption technique offers the advantages of low operating cost, minimization of the less disposed volume of chemical and biological sludge and high efficiency in detoxifying very dilute effluents. These advantages have served as the incentives for developing full biosorption technique to clean up heavy metal pollution. Biosorption technology is just developing rapidly, and is attractting more and more attention from scientists over the world, and we hope this technology will be extensively applied in our country. | |
| 01/01/2003 00:00:00 | |
| Link to Article | |
| 1.3.12 | Biosorption |
| Comparative Study of Rates of Biosorption for Selected Single and Mixed Metal Ions using Natural Products | |
| Heavy metals are usually found in low concentrations in natural aquatic ecosystem. In recent times, however, the occurrence of metal contaminants especially heavy metals in excess of natural loads has become a problem of increasing concern. The contributing factors are rapid growth of population, increased urbanization and expansion of industrial activities, exploration and exploitation of natural resources, extension of irrigation and other modern agricultural practices as well as lack of environmental regulations. This therefore, calls for efficient, cheap, available and non polluting method of controlling presence of heavy metals in water bodies. Use of natural biosorbents such as algae has demonstrated great potential to remove heavy metals from wastewater. An investigation of the effect of contact time, reaction kinetics, influence of ionic sizes and influence of presence of other metal ions in biosorption of heavy metals Cu, Zn and Pb using Ascophyllum nodosum has been done. Model wastewater solution containing a known concentration of the given heavy metal ions was prepared for both single and mixed at a fixed pH of 5. A 0.25g mass of dry algae was introduced for every 100 mL solution. Change in level of concentration was monitored at intervals of 10 minutes using AAS until the rate of biosorption was almost constant. The sorption process occurred in two stages; first being rapid adsorption and then gradual adsorption that was almost constant. Pb was most biosorbed while Zn was least for both systems, adopting the order Pb > Cu > Zn. The data obtained fitted both Langmuir isotherm and experimental parameters were determined. The order of reaction was found to follow pseudo second order after comparison of R2 values that were deduced from first and second order linearized plots.Key words: Biosorption, heavy metals, algae, wastewater, pollution | |
| 01/01/2013 00:00:00 | |
| Link to Article | |
| 1.3.13 | Biosorption |
| Different methods to adsorb heavy metals in wastewater by blue-green algae | |
| Background: Among the today`s main problems related to wastewater is pollution caused by heavy metals. These heavy metals are toxic and have detrimental effects on the body. So the existence of such metals in the food chain is a serious problem for human health. Materials and Methods: Scopus, Pubmed, Google scholar and ScienceDirect databases were searched. Results: Studies indicate a requirement to use a new method for removing heavy metals from wastewater. Biosorption method by microalgae is one of the newest methods which have the properties such as cost, selective adsorption, high processing rate and no sludge production. In this process in order to clean up wastewater by adsorption, the two algae Chlorella and Spirulina are optimal. In comparing these two algaes, Chlorella algaehas better ability to attract as well as more balanced with the absorption effect. Remove ions such as lead, nickel and zinc occurs by interactions between the metal ions and carboxyl groups present on the cell wall that stabilize metal binding. Notable point in this process is that the removal ability decreases by increasing the metal concentration. In addition, Chlorella can be used to adsorb Chromium that Betacaroten first extracted and then the remaining biomass is used for Chromium adsorption. Conclusions: According to the case studies, the method is convenient and cost effective for the removal of metal contaminants from wastewater and will help to reduce environmental pollution. | |
| 03/15/2013 00:00:00 | |
| Link to Article | |
| 1.3.14 | Biosorption |
| Fungal-Based Nanotechnology for Heavy Metal Removal | |
| Heavy metal pollution, cleaning and recycling are a major environmental issue. In particular, there is a need for efficient techniques to treat wastewaters. Conventional technologies to treat industrial waters are limited by stringent health policies and emerging contaminants. Fungi-based nanotechnology is rapidly emerging as an effective technology to treat industrial wastewaters. This chapter reviews the recent developments in fungal biosorption, biological synthesis of nanoparticles using fungi, and the application of fungi-based nanosorbents for heavy metals removal. | |
| 01/01/2018 00:00:00 | |
| Link to Article | |
| 1.3.15 | Biosorption |
| Keratin Protein Nano-fiber for Removal of Heavy Metals and Contaminants | |
| ABSTRACT Keratin protein fiber (AKF TM ) is a renewable source of biosorbent that can be used for filtration of heavy metal and nanosize contaminants. The major composition of keratin fiber is the structured protein micofibril, consisting of numerous nanosized pores. The combination of nanostructure and metal binding capacity protein sites make it an ideal material for removal of heavy metals from solutions. The mechanism of heavy metal uptake onto keratin protein involves a combination of several steps such as adsorption, precipitation, and ion exchange. Keratin protein has good tensile strength and is stable over a wide pH range. INTRODUCTION & BACKGROUND Conventional methods for removing heavy metals from contaminated solutions include chemical precipitation, carbon adsorption, membrane separation, microfiltration and the use of ion exchange resins. Many of the existing technologies for the removal of heavy metals from wastewaters are unable to achieve the low final concentrations required by new regulations. Furthermore, many existing treatment processes merely convert aqueous metal ions into solid sludges, which require costly landfill disposal. Biosorption, a relatively simple metal adsorption process, can meet the progressively stricter environmental discharge criteria. The term "biosorption" is used to describe the accumulation of metal ions by adsorption and/or ion exchange from solutions by materials of biological origin, particularly microorganisms, plant biomass and animal cells and extracts [1]. Thus the potential use of materials of biological origin in the treatment of heavy metal-contaminated wastewaters is of special importance. Organisms such as algae, bacteria, fungi, and yeasts have proved to be potential metal sorbents [1] | |
| 01/01/2001 00:00:00 | |
| Link to Article | |
| 1.3.16 | Biosorption |
| Microbial Biosorption as a Green Technology for Bioremediation of Heavy Metals. | |
| The exponential growth of Industrialization with the increase in human population has led to a heavy metal pollution problem, which has become ubiquitous from air to soil. Heavy metal pollution has become a more serious environmental problem in the last several decades as a result of its toxicity and insusceptibility to the environment. There are many bioremediation technologies including biosorption process to decontaminate the heavy metal polluted sites. Biosorption is a technique that can be used for the removal of pollutants from waters, especially those that are not easily biodegradable such as metals and dyes. A variety of biomaterials are known to bind these pollutants, including bacteria, fungi, algae, and industrial and agricultural wastes. In this review, the biosorption abilities of bacterial and fungal biomass towards metal ions are emphasized. This review attempts to present a brief summary of the role of biosorption in heavy metal removal from wastewater. Undoubtedly, the biosorption process is a potential technique for heavy metal decontamination. | |
| 01/01/2015 00:00:00 | |
| Link to Article | |
| 1.3.17 | Biosorption |
| Potential of biosorption and bioaccumulation processes for heavy metals removal in bioreactors | |
| Environmental contamination with heavy metals, especially of soils and water, became a significant problem because most of them are toxic to the living organisms, non-degradable and persistent in the contaminated media. Physico-chemical methods, such as chemical precipitation, electrochemical treatment, filtration, ion exchange, evaporation, reverse osmosis and membrane technologies are currently the most used methods to remove heavy metal ions from wastewaters. Bioremediation technologies, which are known to be environmentally sound natural processes, have become attractive alternatives to the conventional methods. Among these, biosorption and bioaccumulation address various interactions and concentration of toxic metals in either living (bioaccumulation) or non-living (biosorption) biomass. The aim of this paper is to emphasize the proficiency of biosorption and bioaccumulation processes applied in different types of bioreactors (stirred tank, fixed bed, fluidized-bed and air-lift) using various microorganisms for the removal of heavy metals from contaminated effluents. | |
| 11/01/2015 00:00:00 | |
| Link to Article | |
| 1.3.18 | Biosorption |
| Removal of chromium (VI) by Escherichia coli cells expressing cytoplasmic or surface-displayed ChrB: a comparative study. | |
| Various genetically engineered microorganisms have been developed for the removal of heavy metal contaminants. Metal biosorption by whole-cell biosorbents can be enhanced by overproduction of metal-binding proteins/peptides in the cytoplasm or on the cell surface. However, few studies have compared the biosorption capacity of whole cells expressing intracellular or surface-displayed metal-adsorbing proteins. In this study, several constructs were prepared for expressing intracellular and surface-displayed Ochrobactrum tritici 5bvl1 ChrB in Escherichia coli BL21(DE3) cells. E. coli cells expressing surface-displayed ChrB removed more Cr(VI) from aqueous solutions than cells with cytoplasmic ChrB under the same conditions. However, intracellular ChrB was less susceptible to variation in extracellular conditions (pH and ionic strength), and more effectively removed Cr(VI) from industrial wastewater than the surface-displayed ChrB at low pH (<3). An adsorption-desorption experiment demonstrated that compared with intracellular accumulation, cell-surface adsorption is reversible, which allows easy desorption of the adsorbed metal ions and regeneration of the bioadsorbent. In addition, an intrinsic ChrB protein fluorescence assay suggested that pH and salinity may influence the Cr(VI) adsorption capacity of ChrB-expressing E. coli cells by modulating the ChrB protein conformation. Although the characteristics of ChrB may not be universal for all metal-binding proteins, our study provides new insights into different engineering strategies for whole-cell biosorbents for removing heavy metals from industrial effluents. | |
| 03/20/2020 00:00:00 | |
| Link to Article | |
| 1.3.19 | Biosorption |
| State of the art for the biosorption process--a review. | |
| In recent years, biosorption process has become an economic and eco-friendly alternative treatment technology in the water and wastewater industry. In this light, a number of biosorbents were developed and are successfully employed for treating various pollutants including metals, dyes, phenols, fluoride, and pharmaceuticals in solutions (aqueous/oil). However, still there are few technical barriers in the biosorption process that impede its commercialization and thus to overcome these problems there has been a steadily growing interest in this research field. This resulted in large numbers of publications and patents each year. This review reports the state of the art in biosorption research. In this review, we provide a compendium of know-how in laboratory methodology, mathematical modeling of equilibrium and kinetics, identification of the biosorption mechanism. Various mathematical models of biosorption were discussed: the process in packed-bed column arrangement, as well as by suspended biomass. Particular attention was paid to patents in biosorption and pilot-scale systems. In addition, we provided future aspects in biosorption research. | |
| 07/01/2013 00:00:00 | |
| Link to Article | |
| 1.3.20 | Biosorption |
| Synthesis of biosorbents from natural/agricultural biomass wastes and sustainable green technology for treatment of nanoparticle metals in municipal and industrial wastewater | |
| Abstract Municipal and industrial wastewaters, manufacturing of electrical and electronic equipment, etc., are spreading toxic heavy metals such as lead, arsenic, zinc, nickel, cadmium, uranium, and mercury in the aquatic and soil environment. There are some traditional treatment technologies to remove heavy metals from drinking water and wastewater. However, conventional treatment technologies are expensive and not always efficient for the treatment of wastewaters with high metal concentration. Furthermore, these methods need more chemicals and energy and produce toxic sludge. By contrast, bioremediation by biosorption process using biosorbents is a low-cost, highly efficient, easy operating, eco-friendly, and sustainable green technology for the removal of heavy metals from wastewater. The renewable biocomposite biosorbent materials can be prepared from plant biomass; agricultural wastes such as fruit peels, straw, and coconut coir; bacteria; yeasts; fungi; and algae. The main mechanisms of biosorption process involve ion exchange, surface complexation, adsorption, absorption, and precipitation methods. Biosorption has several benefits, such as selective removal of metals, biosorbent regeneration and metal recovery, rapid kinetics of adsorption and desorption, and no sludge generation. The biosorbent materials can be modified by different physical and chemical treatments and other treatments to prepare novel adsorbents and remove nanoparticle heavy metal contaminants from wastewater. The biosorbents without treatment have shown low adsorption capacity. The chemical pretreatments significantly improved the adsorption capacities of biosorbents by increasing the number of binding sites, ion-exchange ability, and new functional groups. The main composition of plant biomass and agricultural waste consists of cellulose, hemicellulose, and lignin containing different functional groups, such as hydroxyl groups, acetamido, carboxyl, phenolic, structural polysaccharides, amido, amino, sulfhydryl and carboxyl groups, alcohols, and ester. Some important physical and chemical factors influencing the biosorption of heavy metals from wastewater are pH, temperature, initial heavy metal concentration, biosorbent dose, biosorbent size, ionic strength, and coions. Nanoparticle heavy metals can be recovered from the biosorbents by physical treatment such as heating, stirring, and agitation or chemical treatments. The chemical treatments use the chemicals as eluents that include acid, alkali, and organic solvent. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
2. Electro-treatment
BackTreatments using electrical currents
2.1 Electrocoagulation
Electrocoagulation (EC), is a technique used for wastewater treatment, wash water treatment, industrial processed water, and medical treatment. Electrocoagulation has become a rapidly growing area of wastewater treatment due to its ability to remove contaminants that are generally more difficult to remove by filtration or chemical treatment systems, such as emulsified oil, total petroleum hydrocarbons, refractory organics, suspended solids, and heavy metals.[\[Wiki\]](https://en.wikipedia.org/wiki/Electrocoagulation)
Electrocoagulation is advanced and innovative method which involves direct interaction between the ions of sacrificial metal anode and the pollutants in the water. The dissolved metal ions from sacrificial anode release in wastewater, coagulate with pollutant in wastewater in a manner similar to the traditionally one where chemicals are added for coagulation. The traditionally used chemicals, alum and ferric salts, liberate both, cations and anions. In electrocoagulation there is no supplemental addition of anions and therefore, no increase in salinity of the treated water. The quantity of sludge produced is smaller than that produced during chemical treatment.[ \[Art. #ARTNUM\]](#article-96077-2203672557)
In the electro-coagulation process the coagulant is generated in situ by electrolytic oxidation and reduction occurring at the appropriately chosen electrodes in an electrochemical reactor. **The evolution of hydrogen bubbles serves to promote flotation in EC reactors.**
This technology has been increasingly used for treatment of different types of industrial wastewater containing: suspended particles, clay and clay minerals, chemical and mechanical polishing waste in wastewater, organic compounds: fats, oils, alcohols and grasses , foodstuff, synthetic detergent effluents, heavy metals, bacteria, algae and larvae, textile wastewater, latex particles, laundry wastewater, decolourization of dye and cotton dye, COD, BODand TOC reduction, tannery wastewater, wastewater from slaughter-houses, **for removing metals such as: Mn, Cu, Zn, Ni, Al, Fe, Co, Sn, Mg, Se, Mo, Ca etc. EC has also been used in removing anions such as: CN-, PO43-, SO42-, NO3-, F- and Cl-.**[\[Art. #ARTNUM\]](#article-96077-2203672557)
**Selectivity depends on anode and on pH:**
* the optimal selection of the electrode material depends on the type of pollutant present in the wastewater. The efficiency of iron, aluminum and stainless steel electrodes in the removal of copper(II), chromium(VI) and nickel(II) from metal plating effluent was studied. It was also reported that Cr(III) precipitation was due to the presence of Fe(OH)3 and its removal could be facilitated by the electro-generated Fe(II), reduced at the cathode. **There are some pollutants, such as phosphorous and some metal cations, which have a specific efficiency of removal that depends on the pH.** [\[Art. #ARTNUM\]](#article-96077-2203672557)
**Advantages/Disadvantages:**
* Advantages:
1. Simple equipment, small land area, low initial investment, low operational costs and easy to operate.
2. The electrolytic process is easily controlled only by varying the applied voltage and current density.
3. Lower maintenance requirements
4. Low quantities of produced sludge, which is easy to dewater and it tends to be readily settable.
5. High efficiency in removing the smallest colloidal particles due to the applied electrical field that sets them in faster motion and thereby facilitates coagulation
6. Possibility for removal of a large variety of multiple contaminants in wastewater.
7. Rarely requires small quantities of chemicals, only for augmentation of the conductivity, so there is no problem with neutralization of excess chemicals and secondary pollutants.
* The main Disadvantages are:
1. Depending on the electrode material, oxide films can form on the cathode which reduce the active electrode surface area and conductivity, reducing the process efficiency.
2. High conductivity of wastewater is required. To lower the cost of electrocoagulation, electro-flocculation, and electro-flotation, it is necessary to minimize the IR drop which will enhance the current efficiency. The IR drop should be minimized by decreasing the distance between the electrode plates, i.e. using a higher number of plates positioned at smaller distances.
3. Maintenance and regular replacement of the sacrificial anodes.
4. Evolution of oxygen at the anodes sometimes represents unwanted leakage of current. This problem can be minimized by the choice of an anodic material that has high over potential for oxygen evolution.
5. In some countries the use of electricity may be expensive. [\[Art. #ARTNUM\]](#article-96077-2203672557)
**Heavy metals:**
* Heavy metals have frequently been detected in metal plating wastewater. **In this study, electrocoagulation method using iron (Fe) and aluminum (Al) electrodes was applied to simultaneously remove four heavy metals (Cu, Ni, Zn, Cr) in artificial metal plating wastewater.** In electrocoagulation experiments using Fe electrodes, the mass of sludge formed was 0.68–2.50 kg/m3 and the amount of energy consumed was 0.37–2.78 kW h/m3, respectively, during the treatment of artificial metal plating wastewater containing four heavy metals in the absence of cyanide, which increased to 3.64–4.74 kg/m3 and 4.80–5.04 kW h/m3 for artificial wastewater in the presence of cyanide. [\[Art. #ARTNUM\]](#article-96077-2995529317)
* Electrocoagulation is an electrochemical technique with many applications. This process has recently attracted attention as a potential technique for treating industrial wastewater due to its versatility and environmental compatibility. **This process has been applied for the treatment of many kinds of wastewater such as landfill leachate, restaurant, carwash, slaughterhouse, textile, laundry, tannery, petroleum refinery wastewater and for removal of bacteria, arsenic, fluoride, pesticides and heavy metals from aqueous environments.** [\[Paper\]](https://link.springer.com/article/10.1186/s40201-015-0233-8)
* This paper has elucidated a technical approach for getting rid of heavy metals and total suspended solids from water using an aluminum electrode. The effect of operational parameters, i.e. current density, inter-electrode distance, operating time, and pH, were studied and evaluated for maximum efficiency. The study corroborates the correlation between current density and removal efficiency. Neutral pH and a low electrode gap have been found to aid the efficacy of the electrocoagulation. The results shows a maximum TSS removal efficiency of 76.6 % at a current density of 5.3 mA/cm2 and contact time of 30 minutes. In the heavy metal remediation, 30 min of process time has exhibited extreme reduction rates of 99 %, 59.2%, and 45.8%, for Cu, Cr, and Zn, respectively.[ \[Art. #ARTNUM\]](#article-96077-2289478449)
**Nutrients:**
* On the other hand, the T-P concentration decreased as a result of the precipitation of aluminum ions and phosphates. The membrane permeation flux increased and the fouling resistance (Rc+Rf) decreased with increasing electric current density. Although the particle size of the anaerobic digestion effluent increased slightly, it was not related directly to the reduced fouling phenomena. The main mechanism for the enhanced flux was attributed to the inorganic particulate produced during electrocoagulation, such as , which acted as a dynamic membrane deposited on the membrane surface.[ \[Art. #ARTNUM\]](#article-96077-1988718668)
* **Water contents of nitrates, phosphates and sulfates were considerably reduced by 77.5, 83.3 and 20.0%, respectively.**[ \[Art. #ARTNUM\]](#article-96077-2114574202)
* Observations from the study indicate that electro-coagulation can remove essentially all the silica, reduces Ca, P, Mg and Al although to a lesser extent and adds some iron to the treated juice.[ \[Art. #ARTNUM\]](#article-96077-217936370)
* To reduce extensive energy costs of the internal recycling for the purpose of denitrification in the advanced wastewater treatment, a post-treatment process using an electro-coagulation to treat nitrate in the secondary effluents is evaluated in this study.[ \[Art. #ARTNUM\]](#article-96077-2044350308)
* This study aimed to apply electro-coagulation method using cylindrical Aluminum electrode in continuous mode to remove total phosphorus (T-P) in municipal wastewater. The effects of NaCl concentration (or conductivity) and hydraulic retention time (HRT, or flow rate) on T-P removal efficiency were investigated. To determine the efficiency of this system the ratio Al consumption/T-P removal was also considered. The results showed that, with raw sewage as influent, HRT = 1.17 min and added NaCl = 0.04 % was found the best conditions for the highest T-P removal efficiency (92.80 %; T-P concentration remainder was 0.17 mg/L) and the ratio Al consumption/T-P removal was 5.0. In general, this method achieves a high efficiency of removing phosphorus from wastewater and it can be used in sewage treatment systems.[ \[Art. #ARTNUM\]](#article-96077-2793466606)
Suppliers
| 2.1.1 | Electrocoagulation |
|---|---|
| Advanced Electrochemical Technologies in Wastewater Treatment Part I: Electrocoagulation | |
| This paper aims to provide an overview of electrochemical technologies in wastewater treatment. Part I focuses on the basic theory development and application of electro-coagulation. Electrocoagulation is advanced and innovative method which involves direct interaction between the ions of sacrificial metal anode and the pollutants in the water. The dissolved metal ions from sacrificial anode release in wastewater, coagulate with pollutant in wastewater in a manner similar to the traditionally one where chemicals are added for coagulation. The traditionally used chemicals, alum and ferric salts, liberate both, cations and anions. In electrocoagulation there is no supplemental addition of anions and therefore, no increase in salinity of the treated water. The quantity of sludge produced is smaller than that produced during chemical treatment. In the first part of the paper is given the importance for saving the fresh water and cleaning of wastewater using traditionally methods as: physical/mechanical methods, chemical methods and biological methods. In the second part the structure of colloids and traditional coagulation widely using in nowadays is presented. In the third part, an overview of detailed electrocoagulation theory, supported by literature survey for application in wastewater treatment plants, is given | |
| 10/29/2015 00:00:00 | |
| Link to Article | |
| 2.1.2 | Electrocoagulation |
| Application of electro-coagulation for the pretreatment of membrane separation of anaerobic digestion effluents | |
| The aim of this study was to confirm the feasibility of the electro-coagulation process as a pre-treatment for the membrane separation of anaerobic digestion effluents to minimize membrane fouling. The reduction of membrane fouling was evaluated according to the number of electrodes (immersed surface area of electrodes), current density and contact time. In the case of the small surface area of electrodes, the increased electric field strength resulted in a soluble COD increase due to the destruction of the microbial flocs and/or cells, whereas large changes in the soluble COD were not observed in the case of the high surface area of electrodes. On the other hand, the T-P concentration decreased as a result of the precipitation of aluminum ions and phosphates. The membrane permeation flux increased and the fouling resistance (Rc+Rf) decreased with increasing electric current density. Although the particle size of the anaerobic digestion effluent increased slightly, it was not related directly to the reduced fouling phenomena. The main mechanism for the enhanced flux was attributed to the inorganic particulate produced during electrocoagulation, such as , which acted as a dynamic membrane deposited on the membrane surface. | |
| 07/31/2014 00:00:00 | |
| Link to Article | |
| 2.1.3 | Electrocoagulation |
| Application of Electrocoagulation and Electrolysis on the Precipitation of Heavy Metals and Particulate Solids in Washwater from the Soil Washing | |
| Soil washing, ex situ mechanical technique, is one of the few permanent treatment alternatives to remove metal contaminants from soils by employing physical separation based on mineral processing technologies to remove discrete particles or metal-bearing particles and/or chemical extraction based on leaching or dissolving process to extract the metals from the soils into an aqueous solution. However, washwater remained from soil washing process contains discrete particulate particles along with heavy metals as solution phase to be treated separately, as well as this process can produce large amount of sludge that requires further treatment, slow metal precipitation, poor settling, the aggregation of metal precipitates. Electrical treatments including electrocoagulation and electrolysis can be effective in removing these substances from washwater. This paper reviews the theoretical models in applying electrocoagulation and electrolysis to remove heavy metals and discrete particulate particles in washwater by examining and comparing the status of washwater treatment technologies which have been undertaken, mostly in the US and EU for the period 1990-2012. | |
| 01/01/2014 00:00:00 | |
| Link to Article | |
| 2.1.4 | Electrocoagulation |
| Electro-clarification of clarified juice to minimise evaporator scale | |
| The removal of silicic acid, calcium phosphate and the sesquioxides is essential for the production of high grade raw sugars. Silicic acid and calcium oxalates are the major compounds causing hard and difficult to remove scale in evaporators. This study investigated the extent to which scale forming ions could be removed from clarified sugarcane juice by electro-coagulation (electro-clarification) using a novel Kaselco reactor fed with DC current. Observations from the study indicate that electro-coagulation can remove essentially all the silica, reduces Ca, P, Mg and Al although to a lesser extent and adds some iron to the treated juice. The direct operating cost of an electro-coagulating unit was estimated at <0.02 cents per pound of raw sugar. | |
| 01/01/2000 00:00:00 | |
| Link to Article | |
| 2.1.5 | Electrocoagulation |
| Improvement of aqueous nitrate removal by using continuous electrocoagulation/electroflotation unit with vertical monopolar electrodes | |
| Summary The present study is to investigate removal of nitrate from water solutions by the Electro-Coagulation-Flotation (ECF) process in continuous operation under different conditions. Experimental results indicated that the maximum nitrate removal was achieved by aluminum–aluminum electrode arrangement as anode–cathode. The increase in current density from 0.4 to 3.2 mA cm −2 increased nitrate removal efficiency from 55 to 96% under optimum conditions of time and pH during the ECF. Continuous operation of the ECF reactor led to an increase of nitrate removal from 37% at a detention time of 10 min–96% at a detention time of 30 min. Mean energy consumption and current efficiency were found to be about 2.66 kWh g −1 NO 3 − and 160%, respectively. | |
| 11/01/2016 00:00:00 | |
| Link to Article | |
| 2.1.6 | Electrocoagulation |
| Modelling and cost evaluation of electro-coagulation processes for the removal of anions from water | |
| Abstract A mathematical model previously proposed by our group has been modified for its application in the modelling of arsenates, nitrates and phosphates electro-coagulation with iron and aluminium. It classifies the coagulant and pollutant species attending to their reactivity in the electro-coagulation process on the basis of the experimental behaviour of the system. The enmeshment of anionic pollutants in a growing coagulant precipitate and their direct precipitation are the mechanisms considered. A good reproducibility of the experimental data is obtained (with r 2 above 0.9) with a small number of parameters. The model has been used to predict the amount of coagulant dose required under given conditions for the removal of the anionic pollutants, which allowed obtaining the costs of the electro-coagulation corresponding to the raw material, iron or aluminium sheets, and the energy costs for their electro-dissolution. Results showed that iron electro-coagulation is cheaper than aluminium electro-coagulation, and that the current density does not have an important influence on the costs within the range studied (0.2–4.0 mA cm −2 ). Attending to the results, arsenate and phosphate removal by electro-coagulation seem to be attractive from the economic point of view. | |
| 04/01/2013 00:00:00 | |
| Link to Article | |
| 2.1.7 | Electrocoagulation |
| Performance evaluation of the electro-coagulation treatment process for the removal of total suspended solids and metals from water | |
| Globalization, industrialization, mining, and uncontrolled population growth have fostered a shortage of potable water. Thus, it has become imperative to understand an effective and reasonable water purification technique. A renewed interest in electrocoagulation has been spurred by the search for reliable water-treatment processes. This paper has elucidated a technical approach for getting rid of heavy metals and total suspended solids from water using an aluminum electrode. The effect of operational parameters, i.e. current density, inter-electrode distance, operating time, and pH, were studied and evaluated for maximum efficiency. The study corroborates the correlation between current density and removal efficiency. Neutral pH and a low electrode gap have been found to aid the efficacy of the electrocoagulation. The results shows a maximum TSS removal efficiency of 76.6 % at a current density of 5.3 mA/cm2 and contact time of 30 minutes. In the heavy metal remediation, 30 min of process time has exhibited extreme reduction rates of 99 %, 59.2%, and 45.8%, for Cu, Cr, and Zn, respectively. During the experiments, electrical conductivity and dissolved solids were found to fluctuate by 5–6 % of the original value. Moreover, kinetic study has also demonstrated for pollutants removal follows first and second order model. | |
| 12/01/2015 00:00:00 | |
| Link to Article | |
| 2.1.8 | Electrocoagulation |
| Purification of Raw Surface Water Using Electro-Coagulation Method | |
| The purification of raw surface water from its organic, inorganic and microbial content using the electro-coagulation method was investigated. Batch coagulation experiments were conducted using the jar-test method. A pair of aluminum electrodes (suspended in the jar) was charged with low voltage current for releasing aluminum ions in the raw water to precipitate the suspended matter. The optimum current density was 0.6325 mA cm−2. The coagulation efficiency was evaluated by determining the turbidity of treated water. The efficiency reduction in raw water turbidity was 90%, leading to a change in water Zeta potential from −85 mV (before treatment) to −40 mV (after treatment), i.e. the particles tended to be destabilized and the coagulation process became predominant. Water contents of nitrates, phosphates and sulfates were considerably reduced by 77.5, 83.3 and 20.0%, respectively. Also, this method is effective in reducing both the total viable bacterial count (TVBC) and total coliforms (TC) by a ratio of 1/104 and 1/103, respectively. | |
| 10/01/2004 00:00:00 | |
| Link to Article | |
| 2.1.9 | Electrocoagulation |
| Removal mechanism of heavy metal (Cu, Ni, Zn, and Cr) in the presence of cyanide during electrocoagulation using Fe and Al electrodes | |
| Abstract Heavy metals have frequently been detected in metal plating wastewater. In this study, electrocoagulation method using iron (Fe) and aluminum (Al) electrodes was applied to simultaneously remove four heavy metals (Cu, Ni, Zn, Cr) in artificial metal plating wastewater. The Fe electrode showed greater removal efficiency for especially Cr than did the Al electrode due to the reduction of Cr6+ ion by Fe2+ ions produced from electrode. Alkaline pH favored electrocoagulation because of the abundance of hydroxide (OH−) ions; thus, metal hydroxides can be formed readily under alkaline pH. The metal removal increased with current density, as Fe2+ ion was generated more effectively at high current. However, the electrolyte concentration did not significantly affect metal removal efficiency. In electrocoagulation experiments using Fe electrodes, the mass of sludge formed was 0.68–2.50 kg/m3 and the amount of energy consumed was 0.37–2.78 kW h/m3, respectively, during the treatment of artificial metal plating wastewater containing four heavy metals in the absence of cyanide, which increased to 3.64–4.74 kg/m3 and 4.80–5.04 kW h/m3 for artificial wastewater in the presence of cyanide. The FTIR spectra of the sludge samples generated when using Fe and Al electrodes showed that all four metals exhibited OH stretching peaks, implying that main removal mechanism of metals during electrocoagulation is the precipitation with metal hydroxide. Iron sludge was composed mainly of Fe3O4 and FeO(OH), and Al sludge was mostly AlO(OH). When using Fe electrode in the presence of cyanide, cyanide was also adsorbed onto iron sludge via Fe-CN bonding. | |
| 02/01/2020 00:00:00 | |
| Link to Article | |
| 2.1.10 | Electrocoagulation |
| REMOVAL OF HEAVY METALS FROM INDUSTRIAL WATER USING ELECTRO-COAGULATION TECHNIQUE | |
| Heavy metal removal by electrocoagulation using iron electrodes material was investigated in this paper. Several working parameters, such as pH, current density and heavy metal ions concentration were studied in an attempt to achieve a higher removal capacity. A simple and efficient treatment process for removal of heavy metals is essentially necessary. The continuous flow electrocoagulation system, with reactor consists of a ladder series of twelve electrolytic cells, each cell containing stainless steel cathode and iron anode. The treatment of synthetic solutions containing Zn 2+ , Cu 2+ , Ni 2+ , Cr 3+ , Cd 2+ and Co 2+ has been investigated. | |
| 01/01/2008 00:00:00 | |
| Link to Article | |
| 2.1.11 | Electrocoagulation |
| Removal of heavy metals from mining impacted water by an electrocoagulation-ultrafiltration hybrid process | |
| In this study, the use of an electrocoagulation-ultrafiltration (EC-UF) hybrid system for the treatment of mining impacted wastewater was investigated. A model wastewater solution containing copper, lead, cadmium and other constituents representative of mining impacted wastewater was used in this investigation. The effects of key operational parameters including electrolysis time, current density, and solution pH on the performance of the EC and EC-UF systems were systematically investigated. The removal rates of copper and lead by the EC process were consistently higher than that of cadmium. It is probable that the removal mechanism of cadmium was different from that of the base metal copper and lead. Results reported here indicate that an EC-UF hybrid system could be very effective in removing heavy metals at high solution pH. At an acidic condition, the removal efficiency of heavy metal by both EC and UF reduced dramatically. However, the overall removal efficiency by the hybrid EC-UF system remained q... | |
| 11/01/2009 00:00:00 | |
| Link to Article | |
| 2.1.12 | Electrocoagulation |
| Removal of nitrogen and phosphorus of the secondary effluent by electro-coagulation | |
| To reduce extensive energy costs of the internal recycling for the purpose of denitrification in the advanced wastewater treatment, a post-treatment process using an electro-coagulation to treat nitrate in the secondary effluents is evaluated in this study. Removals of phosphorus and organics in the secondary effluents by the electro-coagulation were also evaluated to propose an alternative advanced wastewatert treatment process. A series of experiments of the electro-coagulation were carried out with the following 4 different samples: synthetic solution containing nitrate only, synthetic solution containing nitrate as well as phosphorus, secondary effluents from activated sludge cultivated in laboratory, and secondary effluents from real wastewater treatment plants. Removals of nitrate and phosphorus in the synthetic solution were 30 and 97 % respectively, which verified the feasibility of the process. Removals of nitrate, phosphorus and COD in the secondary effluents from the cultivated sludge in laboratory were 49, 90 and 19 % respectively. Removal efficiency of the total nitrogen, nitrrate, phosphorus and COD in the secondary effluent from real wastewater treatment plant were 50, 61, 98 and 80 % respectively. The removal of the total nitrogen was less than the nitrate as expected, which is due to the formation of ammonia nitrogen in the cathode. But the proposed scheme could be an energy saving and alternative process for the advanced wastewater treatment if further studies for the process optimization are carried out. | |
| 08/15/2012 00:00:00 | |
| Link to Article | |
| 2.1.13 | Electrocoagulation |
| REMOVAL OF TOTAL PHOSPHORUS FROM MUNICIPAL WASTEWATER USING CYLINDRICAL ALUMINUM ELECTRODE IN CONTINUOUS MODE | |
| This study aimed to apply electro-coagulation method using cylindrical Aluminum electrode in continuous mode to remove total phosphorus (T-P) in municipal wastewater. The effects of NaCl concentration (or conductivity) and hydraulic retention time (HRT, or flow rate) on T-P removal efficiency were investigated. To determine the efficiency of this system the ratio Al consumption/T-P removal was also considered. The results showed that, with raw sewage as influent, HRT = 1.17 min and added NaCl = 0.04 % was found the best conditions for the highest T-P removal efficiency (92.80 %; T-P concentration remainder was 0.17 mg/L) and the ratio Al consumption/T-P removal was 5.0. In general, this method achieves a high efficiency of removing phosphorus from wastewater and it can be used in sewage treatment systems. | |
| 03/22/2018 00:00:00 | |
| Link to Article | |
| 2.1.14 | Electrocoagulation |
| The innovative use of electrocoagulation-microwave techniques for the removal of pollutants from water | |
| Electrocoagulation (EC) is an effective water and wastewater treatment technology; where the coagulants are generated in-situ by electrolytic oxidation of a sacrificial anode. In this technique, pollutant removal is done without adding chemicals; therefore, it remarkably reduces the sludge produced, and consequently reduces the cost of sludge handling. This method has been efficiently used to remove, up to 99%, of a wide range of pollutants such as heavy metals, oil, dyes, and fluoride. However, the EC technology still has a deficiency in the variety of reactor design, and its performance is highly influenced by the chemistry of the water being treated, especially the presence of organic matter (OM), as this inhibits heavy metal removal due to the formation OM-heavy metals complexes. The presence of heavy metals and OM in water resources is one of the most problematic pollutants in Hilla River, Babylon city, Iraq, which inhibits the application of the EC method in that area. Thus, the current study has been devoted to develop a new hybrid EC rector that can be applied to treat water drawn from Hilla River especially, and to treat water containing OM-heavy metals complexes. The aims of this study are therefore; firstly to examine the removal of heavy metals from drinking water in the presence of OM-heavy metal complexes using a new hybrid treatment method that utilises a combination of microwave-electrocoagulation (MW assisted-EC method). Secondly, to present a new configuration for an electrocoagulation reactor (FCER) that employs perforated plate flow columns (which are widely used in the chemical industry) to achieve water mixing, aeration, and temperature control processes. Additionally, the development of statistical models for the EC performance, recovery of hydrogen gas, and the removal of biological pollutants are other targets in the present project. Initially, the performance of the new flow column EC reactor (FCER) was validated in terms of water mixing efficiency, water aeration, and temperature controllability. The results were compared to those of traditional EC reactors. Then, the ability of the FCER to work as an EC unit was validated by treating different pollutants such as fluoride, nitrate, iron, and reactive black 5 (RB-5) dye from drinking water. Then, the ability of the new MW assisted-EC method to remove OM-heavy metal complexes was experimentally proved by treating synthetic water samples contain iron (Fe2+) ions and ethylenediaminetetraacetic acid (EDTA) (C10H16N2O8) (as organic matter). The results obtained showed that FCER achieved a complete water mixing efficiency, and increased the dissolved oxygen (DO) concentration by 110.6% within 10 min, and kept the temperature of water being treated within the range of 22-28 oC for 30 min of electrolysing. While the traditional reactors achieved water-mixing efficiency of 96.5%, increased the DO by 52.2%, and the temperature increased to about 32 oC over the same treatment period. Additionally, FCER was able to reduce fluoride, iron, nitrate, and RB-5 dye concentrations by 98%, 99.6%, 95.2%, 98.6%, respectively. In terms of OM-heavy metal complex removal (the novelty of the present work), the results obtained demonstrated that this novel method removes 92% of this refractory complex within 35 min of treatment at a power of 100 W, temperature of 100 oC, initial pH of 6, ID of 5 mm, and CD of 1.5 mA/cm2. While, the traditional treatment (EC only) removed only 69.6% of this complex under the same operating conditions. It is noteworthy to mention, the new MW assisted-EC method achieved 100% removal of culture-able activated sludge microorganisms ASM from drinking water, which could eliminate the need for costly separated biological treatment units. Statistically, empirical models were developed to reproduce the performance of FCER in terms of fluoride, nitrate, RB-5 dye, iron, and iron-EDTA complex removal. The R2 value for the models of fluoride, nitrate, RB-5 dye, iron, and iron-EDTA complex removal were, respectively, 0.823, 0.848, 0.798, 0.868, and 0.923. Economically, it has been found that the preliminary operating cost of the MW assisted-EC method is 0.628 US $/m3. Additionally, it has been found that the generated hydrogen gas from this new method could be used to reproduce about 2.82 kW/m3 of power, which is a promising amount of power on field scale plants. In conclusion, according to the obtained results, the new MW assisted-EC method is a safe promising alternative to the complicated, expensive, and time consuming traditional treatment methods, as it removes heavy metals in the presence of OM in a relatively short time without the need for chemical additives. Economically, the MW assisted-EC method reduces the need for separated biological treatment unit that require space, money, equipment, and time, because drinking water will be sterilised as it passes through the microwave field. The latter merit makes this new method a cost-effective alternative. Additionally, FCER reduces the need for external mixing and aeration devices that require extra power to work, which makes FCER a cost-effective alternative for traditional lab-scale EC units. | |
| 01/01/2017 00:00:00 | |
| Link to Article | |
| 2.1.15 | Electrocoagulation |
| Resource reuse-type industrial waste water treatment method and apparatus utilizing oxidizing agent generated by utilizing waste | |
|
1. A resource-recycling method of treating industrial wastewater using an oxidizing agent produced from wastewater to decrease amounts of a nitrogen pollutant (T-N), including an ethanolamine compound and ammonia nitrogen (NH3 --N), and a refractory COD (Chemical Oxygen Demand)-causing pollutant in industrial wastewater, the method comprising: stripping ammonia from raw wastewater; producing sodium persulfate in a manner in which the stripped ammonia is placed in a scrubber and added with a sulfuric acid solution diluted to 5 to 50 wt % to thus recover ammonium sulfate concentrated to 5 to 45 wt %, after which the recovered ammonium sulfate and a sulfuric acid solution are fed into an electrochemical conversion unit comprising a diaphragm electrical reactor having an ion exchange membrane to produce ammonium persulfate, after which the produced ammonium persulfate is allowed to react with sodium hydroxide in a reaction chamber; and performing chemical treatment in a manner in which the produced sodium persulfate is added back to the raw wastewater from which ammonia was stripped, thus removing the nitrogen pollutant (T-N) and the refractory COD-causing pollutant. 2. The resource-recycling method of claim 1 , wherein the producing the sodium persulfate comprises stripping ammonia generated during a reaction using a gas-stripping unit to thus recover concentrated ammonium sulfate, or further stripping the ammonia so as to be converted into nitrogen. 3. The resource-recycling method of claim 1 , wherein the diaphragm electrical reactor comprises an anode configured such that a conductive base is coated with at least one selected from among platinum (Pt), iridium (Jr), ruthenium (Ru), tantalum (Ta), tin (Sn) and boron-doped diamond, and a cathode composed of at least one selected from a material used for the anode, titanium (Ti), nickel (Ni), graphite, lead (Pb) and zirconium (Zr), and a surface of the anode or the cathode is in a mesh or plate form. 4. The resource-recycling method of claim 1 , wherein the stripping the ammonia from the raw wastewater comprises adding the raw wastewater with a NaOH aqueous solution so that the raw wastewater has a pH of 9 to 13, and then stripping the ammonia using a gas-stripping unit. 5. The resource-recycling method of claim 1 , further comprising performing intermediate treatment, which comprises physicochemical treatment using a pH control and coagulation chamber in a manner in which the raw wastewater from which ammonia was stripped is added with at least one selected from among an aluminum sulfate-based flocculant, an iron sulfate-based flocculant, an inorganic flocculant and an organic flocculant and thus a pH of the raw wastewater is adjusted, and the raw wastewater is added with a coagulant, so that an organic material and an SS (Suspended Solid) component in the raw wastewater are coagulated, precipitated and separated, and only a supernatant is discharged, before the performing the chemical treatment. 6. The resource-recycling method of claim 5 , wherein the intermediate treatment further comprises electrochemical treatment in a manner in which the raw wastewater composed of the supernatant is electrolyzed through a reaction for 10 to 600 min at a current density of 0.001 to 0.4 A/cm2 , after the physicochemical treatment. 7. The resource-recycling method of claim 5 , further comprising performing electrochemical treatment in a manner in which the raw wastewater subjected to the physicochemical treatment and the chemical treatment is electrolyzed through a reaction for 10 to 600 min at a current density of 0.001 to 0.4 A/cm2 , thus producing a sulfur oxide radical, which is then used to additionally remove a refractory pollutant. 8. The resource-recycling method of claim 1 , further comprising subjecting the raw wastewater, from which ammonia was stripped, to intermediate treatment or post-treatment including at least one treatment selected from among physicochemical treatment for pH control and coagulation precipitation using at least one selected from among an aluminum sulfate-based flocculant, an iron sulfate-based flocculant, an inorganic flocculant and an organic flocculant; biological treatment using microorganisms; physical treatment via filtration and reverse osmosis (RO); electrochemical treatment via electrolysis, electro- coagulation and electro-precipitation; and advanced treatment using ozone (O3 ), reverse electro-osmosis, UV irradiation and sonication, before or after the performing the chemical treatment. 9. A resource-recycling apparatus for treating industrial wastewater using an oxidizing agent produced from wastewater to decrease amounts of a nitrogen pollutant (T-N), including an ethanolamine compound and ammonia nitrogen (NH3 --N), and a refractory COD-causing pollutant in industrial wastewater, the apparatus comprising: a gas-stripping unit for stripping ammonia from raw wastewater; a sodium persulfate production unit, comprising a scrubber configured such that ammonia stripped from the raw wastewater is allowed to react with a sulfuric acid solution diluted to 5 to 50 wt % to thus recover ammonium sulfate concentrated to 5 to 45 wt %, an electrochemical conversion unit comprising a diaphragm electrical reactor having an ion exchange membrane and configured such that the recovered ammonium sulfate is electrochemically reacted and thus converted into ammonium persulfate, and a chemical reaction chamber configured such that the ammonium persulfate thus produced is allowed to react with sodium hydroxide to produce sodium persulfate; and a chemical reaction unit configured such that the raw wastewater, from which ammonia was stripped using the gas-stripping unit, and the sodium persulfate produced using the sodium persulfate production unit are allowed to react so as to remove the nitrogen pollutant (T-N) and the refractory COD-causing pollutant. 10. The resource-recycling apparatus of claim 9 , wherein the sodium persulfate production unit further comprises a gas-stripping unit for stripping ammonia generated upon producing the sodium persulfate. 11. The resource-recycling apparatus of claim 10 , wherein the electrochemical conversion unit is a diaphragm electrical reactor comprising an anode configured such that a conductive base is coated with at least one selected from among platinum (Pt), iridium (Ir), ruthenium (Ru), tantalum (Ta), tin (Sn) and boron-doped diamond, and a cathode composed of at least one selected from a material used for the anode, titanium (Ti), nickel (Ni), graphite, lead (Pb) and zirconium (Zr), and a surface of the anode or the cathode is in a mesh or plate form. 12. The resource-recycling apparatus of claim 9 , further comprising at least one of an intermediate treatment unit and a post-treatment unit disposed before or after the chemical reaction unit. 13. The resource-recycling apparatus of claim 12 , wherein the intermediate treatment unit comprises a pH control and coagulation chamber for treating the raw wastewater from which ammonia was stripped, and an electrolysis chamber, which are sequentially disposed. 14. The resource-recycling apparatus of claim 12 , wherein the post-treatment unit comprises an electrolysis chamber for electrolyzing the raw wastewater to produce a sulfur oxide radical having high oxidation potential. 15. The resource-recycling apparatus of claim 12 , wherein the intermediate treatment unit or the post-treatment unit comprises at least one treatment unit selected from among a pH control and coagulation chamber for physicochemical treatment using at least one selected from among an aluminum sulfate-based flocculant, an iron sulfate-based flocculant, an inorganic flocculant and an organic flocculant; a reaction chamber for biological treatment using microorganisms; a filtration and reverse osmosis chamber for physical treatment through filtration and reverse osmosis (RO); an electrolysis chamber for electrochemical treatment through electrolysis, electro-coagulation and electro-precipitation; and a reaction chamber for advanced treatment using ozone (O3 ), reverse electro-osmosis, UV irradiation and sonication. |
|
| 12/23/2016 00:00:00 | |
| Link to Patent | |
3. Biological
BackBiological system for contaminant removal
3.1 Bioleaching
Bioleaching is the extraction of metals from their ores through the use of living organisms. [\[Wiki\]](https://en.wikipedia.org/wiki/Bioleaching)
It has also been developed for sludge treatment.
Biological Nutrient Removal (BNR) is a process used for nitrogen and phosphorus removal from wastewater before it is discharged into surface or ground water. [\[Source\]](https://www.wateronline.com/doc/biological-nutrient-0001#:\~:text=Biological%20Nutrient%20Removal%20(BNR)%20is,into%20surface%20or%20ground%20water.)
**Bioleaching and bioaccumulation can be used in different formats and reactors, to remove nutrients, minerals or heavy metals from wastewaters, sludges, slurries and soils.**
**Combined removal findings:**
* This study evaluated the capability of **metal biosorption by wasted biomass from a combined anaerobic-anoxic-oxic (A2O)-biofilm process with simultaneous nitrogen and phosphorus removal.** [\[Paper\]](https://europepmc.org/article/med/16112569)
* For the effective application of a modified packed bed biofilm reactor (PBBR) in wastewater industrial practice, it is essential to distinguish the tolerance of the system for heavy metals removal. The industrial contamination of wastewater from various sources (e.g. Zn, Cu, Cd and Ni) was studied to assess the impacts on a PBBR. This biological system was examined by evaluating the tolerance of different strengths of composite heavy metals at the optimum hydraulic retention time (HRT) of 2 hours. The heavy metal content of the wastewater outlet stream was then compared to the source material. Different biomass concentrations in the reactor were assessed. The results show that the system can efficiently treat 20 (mg/l) concentrations of combined heavy metals at an optimum HRT condition (2 hours), while above this strength there should be a substantially negative impact on treatment efficiency.[\[Paper\]](https://journals.plos.org/plosone/article?id=10.1371/journal.pone.0155462)
* The main application and purpose of the modified Bardenpho process is nutrient removal. Meanwhile, due to the utilization of 5 biological stages, removing other impurities such as chemical oxygen demand (COD), biological oxygen demand (BOD), total suspended solids (TSS), heavy metals, and viruses can be considered as added benefits of the modified Bardenpho process.[\[Badenpho process\]](https://link.springer.com/content/pdf/10.1007%2F978-3-319-73645-7_87.pdf)
* The biologically performed solubilization of phosphorus from sewage sludge incineration ash is accompanied by the release of toxic metals. Therefore a combined process to separate phosphorus from heavy metals by achieving a plant available phosphorus-enriched product and a metal depleted ash was designed. Leaching experiments were conducted in laboratory scaled leaching reactor containing a bacterial stock culture of Acidithiobacillus sp.. Next step was the enhancement of P-recovery in combining bioleaching with simultaneous bio-P-accumulation by AEDS-population. The uptake of phosphorus in biomass reaches up to 66 % of the mobilized phosphorus by bioleaching. **The combined biologically performed technology of phosphorus leaching and separation from toxic metals by simultaneous bioaccumulation developed in this study is a promising process for economical and ecological recovery of phosphorus from waste solids.**[ \[Art. #ARTNUM\]](#article-96079-2048449249)
**Biomineralization:**
* Biomineralization is a naturally occurring process in living organisms. In this review, we discuss **microbially induced calcium carbonate precipitation (MICP)** in detail. In the MICP process, urease plays a major role in urea hydrolysis by a wide variety of microorganisms capable of producing high levels of urease. We also elaborate on the different polymorphs and the role of calcium in the formation of calcite crystal structures using various calcium sources. Additionally, the environmental factors affecting the production of urease and carbonate precipitation are discussed. This MICP is a promising, eco-friendly alternative approach to conventional and current remediation technologies to solve environmental problems in multidisciplinary fields. Multiple applications of MICP such as **removal of heavy metals** and radionuclides, improve the quality of construction materials and sequestration of atmospheric CO~2~ are discussed. In addition, we discuss other applications such as removal of calcium ions, PCBs and use of filler in rubber and plastics and fluorescent particles in stationary ink and stationary markers. MICP technology has become an efficient aspect of multidisciplinary fields. **Biomineralization of radionuclide and contaminant metals into calcite occurs as competitive co-precipitation reaction in which suitable divalent cations are incorporated into the calcite lattice.** [\[Paper\] ; ](https://springerplus.springeropen.com/articles/10.1186/s40064-016-1869-2)[\[Paper\]](https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3810791/)
**Heavy metals from sludge/manure:**
* Three kinds of mixed culture of acidophilic bacteria were enriched and prepared from natural acid mine drainage and used in bioleaching experiments. The heavy metals (Cu,Zn and Cd) removal from sewage sludge and the improvement of sewage sludge dewaterability in bioleaching processes were investigated. The results showed that all the three prepared mixed culture of acidophilic bacteria could efficiently remove heavy metals from sewage sludge(P0.01). After 12 days of bioleaching, 82.0% of copper and 82.9% of Cd could be removed by the mixed culture of acidophilic bacteria enriched by modified Starkey medium, and 87.5% of zinc could be leached out when inoculating the mixed culture of acidophilic bacteria enriched by 9K medium. [\[Art. #ARTNUM\]](#article-96079-2359122416)
* The purpose of this work was to study the sulfur concentration on bioleaching of heavy metals from pig manure employing indigenous sulfur-oxidizing bacteria. Also, the variations in physicochemical properties of pig manure before and after bioleaching were investigated. The results showed that sulfur concentration significantly affected the rate of acidification, sulfate production and metal solubilization during pig manure bioleaching process. After 12 days of bioleaching, 93%–97% of Zn, 96%–98% of Mn and 48%–94% of Cu were leached out from pig manure, respectively. [\[Paper\]](https://www.sciencedirect.com/science/article/pii/S2405844017339725#:\~:text=In%20the%20bioleaching%20process%2C%20the,efficiency%20during%20the%20bioleaching%20process.)
* During the treatment of sewage, a huge volume of sludge is generated, which is disposed of on land as soil fertilizer/conditioner due to the presence of nitrogen, phosphorus, potassium and other nutrients. However, the presence of toxic heavy metals and other toxic compounds in the sludge restricts its use as a fertilizer. Over the years, bioleaching has been developed as an environmentally friendly and cost-effective technology for the removal of heavy metals from the sludge. The present paper gives an overview of the various bioleaching studies carried out in different modes of operation. The various important aspects such as pathogen destruction, odor reduction and metal recovery from acidic leachate also have been discussed. Further, a detailed discussion was made on the various technical problems associated with the bioleaching process, which need to be addressed while developing the process on a larger scale. [\[Review\]](https://www.researchgate.net/publication/24216809_Bioleaching_of_heavy_metals_from_sewage_sludge_A_review)
* Heavy metals Zn、Cu、Cd、Ni、Pb and Mn in the compressed sludge from Shenyang Northern Sewage Treatment Plant were removed by bioleaching. The results showed that: **the treatment cycle of bioleaching was about 4d, water should be timely separated from sludge; After the treatment of bioleaching, the content of heavy metals in compressed sludge were below that of control standards for pollutants in sludge from agricultural use**(GB4284-1984), which indicated the sludge from the waste water treatment plant treated by bioleaching could be used as agricultural fertilizer; After the treatment of bioleaching, the existence forms of the six heavy metals were mainly restorable and oxidized state. These research results are very helpful to the dispose and reclamation of sludge from waste water treatment plant.[ \[Art. #ARTNUM\]](#article-96079-2047098036)
**Phytoremediation:**
* Since aquatic plants are effective in removing heavy metals from polluted waters, they are generally accepted as heavy metal bioaccumulators. They may have different accumulation capabilities and exhibit dissimilar tolerances of heavy metals. Among them, Lemna gibba was examined as a bioaccumulating plant in this study. The aim was to determine its heavy metal accumulating capability in secondary treatment effluent.[ \[Art. #ARTNUM\]](#article-96079-2150243580)
* Phytoremediation potential of duckweeds (Lemna minuta, Lemna minor) to remove nutrients from simulated wastewater was analyzed. In two separate experiments, the two species were grown for 28 days in waters enriched with nitrate and phosphate to simulate nutrient concentrations of domestic wastewater.[ \[Art. #ARTNUM\]](#article-96079-3007376919)
* After treatment with algae, substantial decreases were observed in electrical conductivity (EC: 40.8–85.9%), biological oxygen demand (BOD: 7.3–52.4%), chemical oxygen demean (COD: 12.0–30.7%), total dissolved solids (TDS: 25.3–79%) and nitrate (13.5–76.8%) in IWW. Furthermore, the cultivation of algae increased the concentrations of dissolved oxygen (DO: 6.0–67.8%).[ \[Art. #ARTNUM\]](#article-96079-2593400527)
* Like plants, algae need large quantities of nitrates and phosphates to support their fast cell cycles. Certain heavy metals are also important for the normal functioning of algae. These include iron (for photosynthesis), and chromium (for metabolism). Because marine environments are normally scarce in these metals, **some marine algae especially have developed efficient mechanisms to gather these heavy metals from the environment and take them up**. These natural processes can also be used to remove certain heavy metals from the environment. [\[Art. #ARTNUM\]](#article-96079-2914099638)
Suppliers
| 3.1.1 | Bioleaching |
|---|---|
| Advances in bioleaching for recovery of metals and bioremediation of fuel ash and sewage sludge | |
| Abstract Bioleaching has been successfully used in commercial metal mining for decades. It uses microbes to biosolubilize metal-containing inorganic compounds such as metal oxides and sulfides. There is a growing interest in using bioleaching for bioremediation of solid wastes by removing heavy metals from ash and sewage sludge. This review presents the state of the art in bioleaching research for recovery of metals and bioremediation of solid wastes. Various process parameters such as reaction time, pH, temperature, mass transfer rate, nutrient requirement, pulp density and particle size are discussed. Selections of more effective microbes are assessed. Pretreatment methods that enhance bioleaching are also discussed. Critical issues in bioreactor scale-up are analyzed. The potential impact of advances in biofilm and microbiome is explained. | |
| 08/01/2018 00:00:00 | |
| Link to Article | |
| 3.1.2 | Bioleaching |
| Bioaccumulation of heavy metals from the secondary treated municipal wastewater by Lemna gibba L. | |
| Since aquatic plants are effective in removing heavy metals from polluted waters, they are generally accepted as heavy metal bioaccumulators. They may have different accumulation capabilities and exhibit dissimilar tolerances of heavy metals. Among them, Lemna gibba was examined as a bioaccumulating plant in this study. The aim was to determine its heavy metal accumulating capability in secondary treatment effluent. Lemna gibba was collected from | |
| 01/01/2009 00:00:00 | |
| Link to Article | |
| 3.1.3 | Bioleaching |
| Bioleaching of heavy metals from sludge after biological treatment of municipal effluent | |
| The article has compared the efficiency of removing heavy metals from the sludge after biological treatment of municipal wastewaters in the course of biological leaching involving heterotrophic and chemotrophic microorganisms and chemical leaching. The article also showed advantages of the bioleaching of metals under conditions of acidogenic heterotrophic metabolism. The efficiency of the leaching of heavy metals from the sludge varies 80% (Zn) to 15% (Cr) and corresponds to the following series: Zn > Mn > Cu > Ni > Cd > Pb > Cr. | |
| 03/01/2013 00:00:00 | |
| Link to Article | |
| 3.1.4 | Bioleaching |
| Bioleaching remediation of heavy metal-contaminated soils using Burkholderia sp. Z-90 | |
| Bioleaching is an environment-friendly and economical technology to remove heavy metals from contaminated soils. In this study, a biosurfactant-producing strain with capacity of alkaline production was isolated from cafeteria sewer sludge and its capability for removing Zn, Pb, Mn, Cd, Cu, and As was investigated. Phylogenetic analysis using 16S rDNA gene sequences confirmed that the strain belonged to Burkholderia sp. and named as Z-90. The biosurfactant was glycolipid confirmed by thin layer chromatography and Fourier-transform infrared spectroscopy. Z-90 broth was then used for bioleaching remediation of heavy metal-contaminated soils. The removal efficiency was 44.0% for Zn, 32.5% for Pb, 52.2% for Mn, 37.7% for Cd, 24.1% for Cu and 31.6% for As, respectively. Mn, Zn and Cd were more easily removed from soil than Cu, Pb and As, which was attributed to the presence of high acid-soluble fraction of Mn, Zn and Cd and high residual fraction of Cu, Pb and As. The heavy metal removal in soils was contributed to the adhesion of heavy metal-contaminated soil minerals with strain Z-90 and the formation of a metal complex with biosurfactant. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 3.1.5 | Bioleaching |
| Bioremediation of Heavy Metal by Algae | |
| Instead of using mainly bacteria, it is also possible to use mainly algae to clean wastewater because many of the pollutant sources in wastewater are also food sources for algae. Nitrates and phosphates are common components of plant fertilizers for plants. Like plants, algae need large quantities of nitrates and phosphates to support their fast cell cycles. Certain heavy metals are also important for the normal functioning of algae. These include iron (for photosynthesis), and chromium (for metabolism). Because marine environments are normally scarce in these metals, some marine algae especially have developed efficient mechanisms to gather these heavy metals from the environment and take them up. These natural processes can also be used to remove certain heavy metals from the environment. The use of algae has several advantages over normal bacteria-based bioremediation processes. One major advantage in the removal of pollutants is that this is a process that under light conditions does not need oxygen. Instead, as pollutants are taken up and digested, oxygen is added while carbon dioxide is removed. Hence, phytoremediation could potentially be coupled with carbon sequestration. Additionally, because phytoremediation does not rely on fouling processes, odors are much less a problem. Microalgae, in particular, have been recognized as suitable vectors for detoxification and have emerged as a potential low-cost alternative to physicochemical treatments. Uptake of metals by living microalgae occurs in two steps: one takes place rapidly and is essentially independent of cell metabolism – “adsorption” onto the cell surface. The other one is lengthy and relies on cell metabolism – “absorption” or “intracellular uptake.” Nonviable cells have also been successfully used in metal removal from contaminated sites. Some of the technologies in heavy metal removals, such as High Rate Algal Ponds and Algal Turf Scrubber, have been justified for some practical application in China and abroad and limitations of these methods in large-scale still exist. As an innovative clean-up technology, it mainly depends on the biosorption and bioaccumulation abilities of algae, and the former is dominated in the whole process of bioremediation. Studies suggest that the constituents of algae cell wall such as alginate and fucoidan which have key functional groups are chiefly responsible for biosorption of heavy metal ions. | |
| 07/01/2012 00:00:00 | |
| Link to Article | |
| 3.1.6 | Bioleaching |
| Bioremediation of Heavy Metal by Algae: Current and Future Perspective | |
| Instead of using mainly bacteria, it is also possible to use mainly algae to clean wastewater because many of the pollutant sources in wastewater are also food sources for algae. Nitrates and phosphates are common components of plant fertilizers for plants. Like plants, algae need large quantities of nitrates and phosphates to support their fast cell cycles. Certain heavy metals are also important for the normal functioning of algae. These include iron (for photosynthesis), and chromium (for metabolism). Because marine environments are normally scarce in these metals, some marine algae especially have developed efficient mechanisms to gather these heavy metals from the environment and take them up. These natural processes can also be used to remove certain heavy metals from the environment. The use of algae has several advantages over normal bacteria-based bioremediation processes. One major advantage of the removal of pollutants is that this is a process that under light conditions does not need oxygen. Instead, as pollutants are taken up and digested, oxygen is added while carbon dioxide is removed. Hence, phytoremediation could potentially be coupled with carbon sequestration. Additionally, because phytoremediation does not rely on fouling processes, odors are much less a problem. Microalgae, in particular, have been recognized as suitable vectors for detoxification and have emerged as a potential low-cost alternative to physicochemical treatments. Uptake of metals by living microalgae occurs in two steps: one takes place rapidly and is essentially independent of cell metabolism – “adsorption” onto the cell surface. The other one is lengthy and relies on cell metabolism – “absorption” or “intracellular uptake.” Nonviable cells have also been successfully used in metal removal from contaminated sites. Some of the technologies in heavy metal removals, such as High Rate Algal Ponds and Algal Turf Scrubber, have been justified for some practical application in China and abroad and limitations of these methods in large-scale still exist. As an innovative clean-up technology, it mainly depends on the biosorption and bioaccumulation abilities of algae, and the former is dominated in the whole process of bioremediation. Studies suggest that the constituents of algae cell wall such as alginate and fucoidan which have key functional groups are chiefly responsible for biosorption of heavy metal ions. | |
| 07/01/2012 00:00:00 | |
| Link to Article | |
| 3.1.7 | Bioleaching |
| Combined approach for soybean wastewater chemical oxygen demand reduction using Aspergillus niger pelletization technology | |
| ABSTRACTUsing biological processes to treat soybean wastewater has great potential, because it generates biomass and reduces sludge production. The formation of Aspergillus niger pellets during cultivation in wastewater has the additional benefit that such pellets are easy to harvest. In the first wastewater treatment step, A. niger pelletization decreased the chemical oxygen demand (COD) by 80.35%. In the second step, A. niger, when combined with added nutrients and cultivated in the presence of Pichia pastoris, did not decrease the COD. Aspergillus niger did not degrade some carbon compounds according to total carbon, organic carbon, and inorganic carbon analysis. The COD decreased from 3.26 × 104 mg O2/L to 616.67 mg O2/L (a 98.11% COD reduction) after activated carbon absorption, which indicates that this approach is efficient. In summary, this study proposes a combined method to treat high-COD-value soybean wastewater. | |
| 03/04/2017 00:00:00 | |
| Link to Article | |
| 3.1.8 | Bioleaching |
| Comparison of bioleaching and electrokinetic remediation processes for removal of heavy metals from wastewater treatment sludge | |
| Abstract Heavy metals prevent the growing amount of sewage sludge from being disposed as fertilizeron land. The electrokinetic remediation and bioleaching technology are the promising methods to remove heavy metals. In recent years, some innovation has been made to achieve better efficiency, including the innovation of processes and agents. This paper reviews the development of the electrokinetic remediation and bioleaching technology and analyses their advantages and limitation, pointing out the need of the future research for the heavy metals-contaminated sewage sludge. | |
| 02/01/2017 00:00:00 | |
| Link to Article | |
| 3.1.9 | Bioleaching |
| Decontamination of heavy metal laden sewage sludge with simultaneous solids reduction using thermophilic sulfur and ferrous oxidizing species | |
| A possibility of using simultaneous sewage sludge digestion and metal leaching (SSDML) process at the thermophilic temperature to remove heavy metals and suspended solids from sewage sludge is explored in this study. Though thermophilic sludge digestion efficiently produces a stable sludge, its inability to remove heavy metals requires it to be used in tandem with another process like bioleaching for metal reduction. Previously, different temperature optima were known for the heterotrophs (thermophilic) responsible for the sludge digestion and the autotrophs involved in bioleaching (mesophilic), because of which the metal concentration was brought down separately in a different reactor. In our study, SSDML process was carried out at 50 °C (thermophilic) by using ferrous sulfate (batch-1) and sulfur (batch-2) as the energy source in two reactors. The concentration of volatile suspended solids reduced by >40% in both batches, while that of heavy metals zinc, copper, chromium, cadmium and nickel decreased by >50% in both batch-1 and batch-2. Lead got leached out only in batch-1. Using 16S rRNA gene-based PCR-denaturing gradient gel electrophoresis analysis, Alicyclobacillus tolerans was found to be the microorganism responsible for lowering the pH in both the reactors at thermophilic temperature. The indicator organism count was also below the maximum permissible limit making sludge suitable for agricultural use. Our results indicate that SSDML at thermophilic temperature can be effectively used for reduction of heavy metals and suspended solids from sewage sludge. | |
| 02/01/2016 00:00:00 | |
| Link to Article | |
| 3.1.10 | Bioleaching |
| Enhanced heavy metal bioleaching efficiencies from anaerobically digested sewage sludge with coinoculation of Acidithiobacillus ferrooxidans ANYL-1 and Blastoschizomyces capitatus Y5. | |
| Prolonged bioleaching period was required to remove heavy metals from anaerobically digested sewage sludge in the presence of low molecular weight organic acids. The purpose of the present study was therefore to enhance metal solubilization efficiencies through introducing organic acid-degrading microorganisms into this artificial bioleaching system. An acetic and propionic acid-degrading yeast Blastoschizomyces capitatus Y5 was successfully isolated from a local Yuen Long sewage sludge and it could achieve optimum growth in synthetic liquid media containing 2,000 mg l-1 acetic acid or 1,000 mg l-1 propionic acid. When it was inoculated simultaneously with Acidithiobacillus ferrooxidans ANYL-1 into anaerobically digested sewage sludge, which contained 648 mg l-1 acetic acid and 731 mg l-1 propionic acid, both acids were completely decomposed within 24 hours. As a result, ferrous iron oxidation was greatly improved, resulting in enhanced metal solubilization. Compared with the 8, 10 and 12 days required for maximum solubilization of Zn, Cu and Cr for the control sludge, the bioleaching period was significantly shortened to 4, 5 and 8 days respectively for sludge receiving co-inoculation. | |
| 11/01/2004 00:00:00 | |
| Link to Article | |
| 3.1.11 | Bioleaching |
| Environment-enhancing process for algal wastewater treatment, heavy metal control and hydrothermal biofuel production: A critical review | |
| Abstract Coupling algae growth on wastewater with hydrothermal liquefaction (HTL) is regarded as an environment-enhancing pathway for wastewater management, biomass amplification, sustainable energy generation and value-added products generation. Through this integrated pathway, microalgae can not only recover nitrogen and phosphorus, but also absorb heavy metals from the wastewater. The migration and transformation of heavy metals need to be specifically assessed and considered due to the environmental concerns associated with metal toxicity. This work reviewed recent advances with respect to bioremediation mechanisms. Particular emphasis was placed on the heavy metal migration, transformation, and the key factors involved in algal wastewater treatment and biomass conversion. Additionally, the challenges of coupling algae wastewater treatment, hydrothermal conversion, and heavy metal control were addressed. Finally, a paradigm involving enhanced algal wastewater treatment and bioenergy production for field application was proposed. | |
| 11/01/2019 00:00:00 | |
| Link to Article | |
| 3.1.12 | Bioleaching |
| Evaluation of microalgae’s (Chlorella sp. and Synechocystis sp.) pollutant removal property: Pig effluent as a live stock discharge - | |
| The ability of microalgae to remove nitrogen and phosphorus from wastewater has been used in recent years as an alternative treatment for discharges from livestock slurry, which generate a negative environmental impact on vulnerable ecosystems. With this background and the feasibility of using microalgae, we have evaluated the effect of Chlorella sp. and Synechocystis sp., in removing contaminants from the pig manure collected from El Prado ESPE. Slurry samples were collected, filtered and autoclaved, and the supernatant was further dilluted to three different concentrations of 40%, 60% and 80%. The microalgal growth and pollutants removal property was evaluated up to 15 days in batch culture. The cell density was determined by counting in a Neubauer hemocytometer, and the pollutants removal was analyzed by standard colorimetric methods. The microalgae Chlorella sp. showed a maximum cell growth of 1.70 ± 0.09 x107 cells/mL at 60% effluent concentration on day 6. While Synechocystis sp. showed a maximum growth of 1.04 ± 0.05 x107 cells/mL, at 60% concentration on day 9. On the other hand, there exists a competition when microalgae used as a consortium. The cell growth of Chlorella sp. was higher at all concentrations compared to Synechocystis sp.. Overall, efficiency of pollutant removal were between 40% and 90%, which demonstrate the feasibility of using microalgae in tertiary swine wastewater treatment. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 3.1.13 | Bioleaching |
| Heavy Metal Removal by Bioaccumulation Using Genetically Engineered Microorganisms | |
| Wastewater effluents from mines and metal refineries are often contaminated with heavy metal ions, so they pose hazards to human and environmental health. Conventional technologies to remove heavy metal ions are well-established, but the most popular methods have drawbacks: chemical precipitation generates sludge waste, and activated carbon and ion exchange resins are made from unsustainable non-renewable resources. Using microbial biomass as the platform for heavy metal ion removal is an alternative method. Specifically, bioaccumulation is a natural biological phenomenon where microorganisms use proteins to uptake and sequester metal ions in the intracellular space to utilize in cellular processes (e.g. enzyme catalysis, signaling, stabilizing charges on biomolecules). Recombinant expression of these import-storage systems in genetically engineered microorganisms allows for enhanced uptake and sequestration of heavy metal ions. This has been studied for over two decades for bioremediative applications, but successful translation to industrial-scale processes is virtually non-existent. Meanwhile, demands for metal resources are increasing while discovery rates to supply primary grade ores are not. This review re-thinks how bioaccumulation can be used and proposes that it can be developed for bioextractive applications – the removal and recovery of heavy metal ions for downstream purification and refining, rather than disposal. This review consolidates previously tested import-storage systems into a biochemical framework and highlights efforts to overcome obstacles that limit industrial feasibility, thereby identifying gaps in knowledge and potential avenues of research in bioaccumulation. | |
| 10/29/2018 00:00:00 | |
| Link to Article | |
| 3.1.14 | Bioleaching |
| Heavy metal removal from contaminated sludge for land application : A review | |
| In recent years, various methods for heavy metal removal from sewage sludge have been extensively studied in order to minimize the prospective health risks of sludge during land application. In this paper, a comparative review and critical analysis of the application of chemical extraction, bioleaching, electroreclamation, and supercritical fluid extraction (SFE), in removing heavy metals from contaminated sludges is presented. Moreover, speciation studies, which can indicate ease of leachability of the different forms of heavy metals in sludge, are also presented. Experimental studies revealed a broad range in metal extraction efficiencies of the different extraction technologies. Acid treatment seemed to effectively remove Cd, attaining as much as 100% removal for some studies, as compared to bioleaching. SFE also gave higher removal efficiency than bioleaching. Cr, Pb and Ni seemed to be also effectively removed by the acid treatment. For the removal of Cu, Mn and Zn, the bioleaching process seemed to be appropriate with maximum removal efficiencies of 91%, 93% and 96% for the three metals, respectively, and as high as 64% minimum removal efficiency for Zn. The SFE process also gave good results for Cu, Mn and Zn removal. Electroreclamation exhibited better removal efficiency for Mn, but is still inferior to acid treatment and bioleaching processes. For chemical extraction, because of the adverse impacts that can result from the use of inorganic acids and complexing agents, interest can be directed more toward utilizing organic acids as extracting agents because of their biodegradability and capability to remove metals at mildly acidic condition, hence requiring less acid. The bioleaching process, although it seems to give a higher yield of metal extraction with lower chemical cost than chemical extraction, may be limited by the inability of the system to cope with the natural environmental conditions, requires strict monitoring of aeration rate and temperature and has applicability to only low sludge solids concentration. A full-scale study would be useful to better assess the efficiency of the process. The electroreclamation technology is limited by its relatively higher energy consumption and limited applicability to sludge. The SFE method, on the other hand, is limited by the complexity of the process and the cost of ligands suitable for effective metal extraction. Both of these technologies are still in their early stage of application and hence there is a need for further basic and applied studies. Finally, the common advantage for almost all treatment technologies studied is that the extraction efficiencies for some metals are high enough to remove metals from sludge to levels suitable for land application. | |
| 01/01/2006 00:00:00 | |
| Link to Article | |
| 3.1.15 | Bioleaching |
| Heavy metals removal from sewage sludge and dewaterability improvement by bioleaching | |
| Three kinds of mixed culture of acidophilic bacteria were enriched and prepared from natural acid mine drainage and used in bioleaching experiments.The heavy metals(Cu,Zn and Cd) removal from sewage sludge and the improvement of sewage sludge dewaterability in bioleaching processes were investigated.The results showed that all the three prepared mixed culture of acidophilic bacteria could efficiently remove heavy metals from sewage sludge(P0.01).After 12 days of bioleaching,82.0% of copper and 82.9% of Cd could be removed by the mixed culture of acidophilic bacteria enriched by modified Starkey medium,and 87.5% of zinc could be leached out when inoculating the mixed culture of acidophilic bacteria enriched by 9K medium.Meanwhile,the bioleaching processes could also significantly enhance sewage sludge dewaterability(P0.01).The centrifugal dehydration efficiency of sewage sludge rose from 73.1% up to 90.0% after 12 days of bioleaching.The microscope observation and energy spectrum analysis demonstrated that the dewaterability improvement of sewage sludge was attributable to the changes of particle structure from flocculent to obvious granular and the formation of the secondary minerals mainly consisting of iron,oxygen and sulfur elements in the bioleaching processes. | |
| 01/01/2013 00:00:00 | |
| Link to Article | |
| 3.1.16 | Bioleaching |
| Immobilizing Microcystis aeruginosa and powdered activated carbon for the anaerobic digestate effluent treatment | |
| Abstract The environment pollution caused by livestock anaerobic digestate effluent (ADE) is becoming increasingly severe recently. In this study, immobilized technology, embedding Microcystis aeruginosa (MA) and powdered activated carbon (PAC) with sodium alginate (SA), was employed to investigate the removal performance of nitrogen (TN), phosphorus (TP) and dissolved organic matter (DOM) in the treatment of ADE solution. Initially, orthogonal experiment was carried out to achieve the optimal conditions of the beads fabrication with the concentration of imbedding agents (PAC-SA) of 5% (w/w) and the ratio of microalgae and imbedding agents was 1:1 (v/v). The results indicated that the total nitrogen (TN), total phosphorus (TP) and total organic carbon (TOC) can be efficiently removed under the optimal operation conditions, with average removals of 91.88 ± 2.91% in TN, 98.24 ± 0.12 in TP and 78.31 ± 1.57% in TOC, respectively. Moreover, the fluorescence excitation-mission matrix (EEM) results illustrated that IMA-PAC beads joined system can efficiently diminish the concentrations of protein-like compounds and humic substances. Therefore, the organic contaminants and nutrients (i.e. N and P) can be efficiently removed in IMA-PAC beads joined system, which would contribute to developing new strategies for the treatment of ADE solution and nutrient recycle. | |
| 04/01/2020 00:00:00 | |
| Link to Article | |
| 3.1.17 | Bioleaching |
| Investigation of municipal and olive mill wastewater co-treatment in activated sludge - powdered activated carbon (AS-PAC) systems | |
| BACKGROUND: The purpose of this study was to investigate the co-treatment of olive-mill wastewater (OMW) and municipal wastewater in activated sludge systems operating in the absence and presence of different adsorbent materials and to study the role of sorption and biodegradation in total phenols removal. RESULTS: Batch experiments were initially conducted to investigate total phenols’ adsorption capacity on activated sludge (AS), olive pomace (OP) and powdered activated carbon (PAC). According to the results, PAC presented the best adsorption capacity. Three sequencing batch reactors (SBRs) were also operated, treating municipal wastewater and different amounts of OMW. The first SBR contained AS (AS-System), the second AS and OP (AS-OP System) and the third AS and PAC (AS-PAC System). All SBRs operated sufficiently in the presence of 1% v/v OMW, achieving mean COD and total phenols removal efficiency higher than 86% and 85%, respectively, and satisfactory settling capacity. Increase of OMW concentration to 5% v/v affected the performance of SBRs, resulting in mean COD removal efficiencies that ranged between 61% (AS-OP System) and 80% (AS-PAC System). CONCLUSION: Among the SBRs used, the AS-PAC System operated with highest performance in the presence of 1 and 2.5% v/v OMW, and showed better stability in the presence of 5% v/v OMW. Calculation of total phenols mass flux revealed that biodegradation was the principal mechanism of their removal. The highest values of mean biotransformation rates were calculated for the AS-PAC System and ranged between 2.0 and 40.6 d −1 for different experimental phases. c � 2012 Society of Chemical Industry | |
| 04/01/2012 00:00:00 | |
| Link to Article | |
| 3.1.18 | Bioleaching |
| Mechanism of high contaminant removal performance in the expanded granular sludge blanket (EGSB) reactor involved with granular activated carbon for low-strength wastewater treatment | |
| Abstract The sludge granulation in an anaerobic bioreactor is rather difficult for treating low-strength wastewater. In this study, an expanded granular sludge blanket (EGSB) reactor involved with granular activated carbon (GAC) was employed to treat wastewater at different operational conditions. In general, a stable COD removal performance was operated at the HRT condition of 8, 6, 5, and 4 h, and V up ranges from 1.09 to 2.44 m h −1 . However, the NH 3 -N removal efficiency was at a relatively low level resulted from the nitrification efficiency was limited to the low dissolved oxygen concentration in anaerobic bioreactor. Adding GAC to the raw sludge, the average size of granular sludge and enzymatic [dehydrogenase activity (DHA) and specific methanogenic activity (SMA)] activities presented an increase trend with the experiment grows. In addition, the promotion of organic load rate (OLR) and V up might stimulate the external mass transfer effect in EGSB reactor, which resulted in the increase of extracellular polymeric substances (EPS) content. DNA sequencing analysis demonstrated that the growth of Aeromonas genus was the main reason for the unstable distribution of acetoclastic and hydrogenotrophic methanogens in HRT condition of 4 h. | |
| 02/01/2018 00:00:00 | |
| Link to Article | |
| 3.1.19 | Bioleaching |
| Phosphorus recovery from sewage sludge ash with bioleaching and electrodialysis | |
| Abstract Phosphorus is an essential element for all living organisms and for plants. However, phosphate rock, which is the main source of phosphorus, is limited and thus it must be recovered from secondary sources like sewage sludge ash (SSA). SSA is one of the most promising secondary sources because it contains considerable amounts of phosphorus. The drawback of SSA as a secondary source is the presence of heavy metals along with phosphorus. In this study, a bioleaching process was applied to solubilize the phosphorus more economically, thus bioleaching bacteria was used to obtain acidic conditions for phosphorus leaching. For this purpose, batch bioleaching experiments were carried out with Sulfur oxidizing bacteria (SOB) to optimize the process in terms of phosphorus dissolution. Experiments were conducted with different amounts of ash, inoculum volumes, and sulfur concentrations. Because the application of the bioleaching process leads to solubilization of heavy metals beside phosphorus, an electrodialysis process was used to separate phosphorus from heavy metals. Electrodialysis experiments were performed in a 3 compartment electrodialysis reactor with gold coated copper electrodes. The maximum phosphorus bioleaching was obtained with 2 g of ash, 40% inoculum, and 10 g.l-1 elemental sulfur. Electrodialysis studies with gold coated copper electrodes lasted for 14 days and 24.6% of the phosphorus was transported to the anode. | |
| 10/01/2019 00:00:00 | |
| Link to Article | |
| 3.1.20 | Bioleaching |
| Phytoremediation potential of the duckweeds Lemna minuta and Lemna minor to remove nutrients from treated waters | |
| Phytoremediation potential of duckweeds (Lemna minuta, Lemna minor) to remove nutrients from simulated wastewater was analyzed. In two separate experiments, the two species were grown for 28 days in waters enriched with nitrate and phosphate to simulate nutrient concentrations of domestic wastewater. Water physical and chemical measurements (temperature, pH, conductivity, oxygen) and plant physiological and biochemical analysis (biomass, relative growth rate–RGR, nutrient and chlorophyll contents, peroxidative damage, bioconcentration factor–BCF) were made to test and compare the phytoremediation capacity of the two Lemna species. L. minuta biomass increased almost tenfold during the time-course of the treatment resulting in a doubling of the mat thickness and a RGR of 0.083 ± 0.001 g/g day. Maximum frond content of phosphate was reached by day 21 (increase over 165%) and nitrate by day 7 (10%). According to the BCF results (BCF > 1000), L. minuta was a hyperaccumulator for both nutrients. On the other hand, L. minor biomass and mat thickness decreased continuously during incubation (RGR = − 0.039 ± 0.004 g/g day). In L. minor fronds, phosphate content increased until day 14, after which there was a decrease until the end of the incubation. Frond nitrate content significantly decreased by day 7, but then remained relatively constant until the end of the experiment. L. minor proved to be hyperaccumulator for phosphates, but not for nitrates. Results indicated L. minuta has a greater potential than L. minor to remove both nutrients by bioaccumulation, especially phosphates, demonstrated also by better physiological and biochemical responses. However, during the incubation, the chlorophyll content of L. minuta mat did continuously decrease and peroxidative damage had increased until day 14, indicating that the system was under some kind of stress. Strategies to avoid this stress were discussed. | |
| 02/22/2020 00:00:00 | |
| Link to Article | |
| 3.1.21 | Bioleaching |
| Remediating industrial wastewater containing potentially toxic elements with four freshwater algae | |
| Abstract The present study was conducted to identify a cost effective method for removal of potentially toxic elements (PTEs) such as cadmium (Cd), chromium (Cr), lead (Pb) and nickel (Ni) from industrial wastewater (IWW), collected from Hayatabad Industrial Estate (HIE), Peshawar, Pakistan. For this purpose, four freshwater algae ( Cladophora glomerata , Oedogonium westii , Vaucheria debaryana and Zygnema insigne ) were used for the treatment of IWW. After treatment with algae, substantial decreases were observed in electrical conductivity (EC: 40.8–85.9%), biological oxygen demand (BOD: 7.3–52.4%), chemical oxygen demean (COD: 12.0–30.7%), total dissolved solids (TDS: 25.3–79%) and nitrate (13.5–76.8%) in IWW. Furthermore, the cultivation of algae increased the concentrations of dissolved oxygen (DO: 6.0–67.8%). The influence was greatly varied among the physicochemical parameters and increased with increasing the incubation time. The bioaccumulation potentials of algae such as C. glomerata , O. westii , V. debaryana and Z. insigne for selected PTEs were ranged from 22.5–80.3, 22.1–63.3, 9.10–92.1 and 17.4–93.0%, respectively. The effect of C. glomerata was highest for Cd (80.3%), whereas O. westti showed the highest removal capacity for Ni (66.3%). The influence of V. debaryana and Z. insigne were highest for Cr followed by Ni. This study revealed that phycoremediation is one of the environmentally friendly and economical feasible techniques used for IWW treatment. | |
| 05/01/2017 00:00:00 | |
| Link to Article | |
| 3.1.22 | Bioleaching |
| Removal of ammonium ions from wastewater A short review in development of efficient methods | |
| ABS TRACT: Ammonium ions wastewater pollution has become one of the most serious environmental problems today. The treatment of ammonium ions is a special concern due to their recalcitrance and persistence in the environment. In recent years, various methods for ammonium ion removal from wastewater have been extensively studied. This paper reviews the current methods that have been used to treat ammonium ion wastewater and evaluates these techniques. These technologies include ion exchange, adsorption, biosorption, wet air oxidation, biofiltration, diffused aeration, nitrification and denitrification methods. About 75 published studies (1979-2015) are reviewed in this paper. It is evident from the literature survey articles that ion exchange, adsorption and biological technology are the most frequently studied for the treatment of ammonium ion wastewater. | |
| 04/01/2015 00:00:00 | |
| Link to Article | |
| 3.1.23 | Bioleaching |
| Removal of Heavy Metals from Sewage Sludge by Bioleaching | |
| This study aims to evaluate the bioleaching process to remove heavy metals from sewage sludge.Sludge acclimatization and bioleaching are both performed on sewage sludge collected from one wastewater treatment plant of Guangzhou. Different sludge inoculation(5%,10%,20%)is added in the treated sludge to study the removal efficiency of heavy metals(Zn,Cd,Pb,Cu).The results show that with the inoculation of 5% of the cultivated sludge,the removal rate of Zn,Cd,Cu and Pb is 46%,54.6%,13.9% and 30.5% respectively,but that of Zn,Cd, Cu and Pb can reach 72%,79.6%,29% and 65.4% respectively.The cultivated sludge mixed liquid had better removal efficiency on heavy metals Zn,Cd and Cu,but lower removal efficiency on Pb,highest only to 29%. | |
| 01/01/2013 00:00:00 | |
| Link to Article | |
| 3.1.24 | Bioleaching |
| Removal of Heavy Metals from Urban Sewage Sludge by Bioleaching | |
| Heavy metals Zn、Cu、Cd、Ni、Pb and Mn in the compressed sludge from Shenyang Northern Sewage Treatment Plant were removed by bioleaching. The results showed that: the treatment cycle of bioleaching was about 4d, water should be timely separated from sludge; After the treatment of bioleaching, the content of heavy metals in compressed sludge were below that of control standards for pollutants in sludge from agricultural use(GB4284-1984), which indicated the sludge from the waste water treatment plant treated by bioleaching could be used as agricultural fertilizer; After the treatment of bioleaching, the existence forms of the six heavy metals were mainly restorable and oxidized state. These research results are very helpful to the dispose and reclamation of sludge from waste water treatment plant. | |
| 11/01/2010 00:00:00 | |
| Link to Article | |
| 3.1.25 | Bioleaching |
| Sequenced Bioleaching and Bioaccumulation of Phosphorus from Sludge Combustion – A New Way of Resource Reclaiming | |
| The recovery of phosphorus from sewage sludge incineration ash as well as the separation of heavy metals from ash was investigated by using the biotechnological process of bioleaching and bioaccumulation of released phosphorus by newly developed population of bioleaching bacteria, Acidithiobacillus sp. strains, and polyphosphate (poly-P) accumulating bacteria, the AEDS-population (Acidithiobacillus sp. enriched digested sludge). The biologically performed solubilization of phosphorus from sewage sludge incineration ash is accompanied by the release of toxic metals. Therefore a combined process to separate phosphorus from heavy metals by achieving a plant available phosphorus-enriched product and a metal depleted ash was designed. Leaching experiments were conducted in laboratory scaled leaching reactor containing a bacterial stock culture of Acidithiobacillus sp.. Next step was the enhancement of P-recovery in combining bioleaching with simultaneous bio-P-accumulation by AEDS-population. The uptake of phosphorus in biomass reaches up to 66 % of the mobilized phosphorus by bioleaching. The combined biologically performed technology of phosphorus leaching and separation from toxic metals by simultaneous bioaccumulation developed in this study is a promising process for economical and ecological recovery of phosphorus from waste solids. | |
| 05/01/2009 00:00:00 | |
| Link to Article | |
| 3.1.26 | Bioleaching |
| The Effect of Microbial Population and Bioregeneration of used GAC in an Activated Sludge Reactor | |
| In the present work an attempt is made to study the role of microbial population on bioregenerationof granular activated carbon (GAC) loaded with phenol compounds in continues bioreactor. The GAC used to treat industrial wastewater of the Mobarakeh steel factory (EsfahanIran), is regenerated by means of biological method. Industrial microbes that obtained from the chemical wastewater treatment unit (in the Mobarakeh steel factory), were used in the bioregeneration process of activated carbon. The relationships between each two important parameters of bioregeneration such as adsorbed phenol, pH, mixed liquor suspended solids (MLSS), total suspended solids (TSS) and sludge volume index (SVI) were studied. It was observed that the adsorption capacity of the bioregenerated GAC increased during the two months of bioregeneration. Furthermore, it was found that pH gradually decreased with degradation of chemical compounds within pores of used GAC. The phenol adsorption capacity increased with increasing microbial cells concentration. In addition, the sludge volume index (SVI) decreased from around 231.11 mL mg -1 to 32.68 mL mg -1 during two months of bioregeneration of used GAC. While microbial concentration increases during thebioregeneration process in continues bioreactor. | |
| 12/22/2012 00:00:00 | |
| Link to Article | |
| 3.1.27 | Bioleaching |
| Treatment technology for brewery wastewater in a water-scarce country: A review | |
| Water is a scarce resource in many parts of the world; consequently the application of innovative strategies to treat wastewater for reuse is a priority. The brewery industry is one of the largest industrial users of water, but its effluent is characterised by high levels of organic contaminants which require remediation before reuse. Various conventional treatment methods such as anaerobic and aerobic systems, which are effective options because of their high removal efficiencies, are discussed in this study. Other methods such as membrane based technologies, carbon nanotubes, activated carbon, electrochemical methods, algal ponds and constructed wetlands are also analysed. Their efficiency as well as advantages and disadvantages are highlighted and evaluated. Combinations of various treatment processes to improve the quality of the final effluent are discussed. | |
| 03/30/2016 00:00:00 | |
| Link to Article | |
4. Membrane technologies
BackTechnologies using membranes
4.1 ultrafiltration
Ultrafiltration (UF) is a pressure-driven barrier to suspended solids, bacteria, viruses, endotoxins and other pathogens to produce water with very high purity and low silt density. Ultrafiltration (UF) is a variety of membrane filtration in which hydrostatic pressure forces a liquid against a semi permeable membrane.[\[Source\]](https://crystalquest.com/pages/what-is-ultrafiltration#:\~:text=Ultrafiltration%20(UF)%20is%20a%20pressure,against%20a%20semi%20permeable%20membrane.)
Polymer-enhanced ultrafiltration (PEUF) is one of the membrane operations that can be used to separate or concentrate heavy metal from liquid streams. It is also called polymer-assisted ultrafiltration (PAF), complexation-ultrafiltration process (CUFP), or polymer-supported ultrafiltration (PSU) [\[Paper\]](https://link.springer.com/referenceworkentry/10.1007%2F978-3-662-44324-8_650)
Ultrafiltration membrane process can separate compounds between 0.005 ≈ 10 μm which is between MF and RO. UF membranes are highly prominent water filters with low energy consumption in removal of pathogenic microorganisms, macromolecules and suspended maters among others. However, UF has some limitations including its inability to remove any dissolved inorganic substances from water and regular cleaning to maintain high pressure water flow[\[Paper\]](https://www.intechopen.com/books/wastewater-and-water-quality/wastewater-treatment-using-membrane-technology)
* Application of membrane technology is one such option which can improve the recycled water quality by removal of heavy metal contaminates, COD, TSS, colour, AOX, and lignin. This shall reduce the load on conventional recovery evaporation system with no significant loss of inorganic compounds. [\[Art. #ARTNUM\]](#article-96074-2992841670)
**Complexation/Ultrafiltration**
* Flocculation/filtration: Based on this concept, we developed an integrated process taking advantage of the **strong adsorption abilities of in-situ Al or Fe hydrolytic flocs and excellent separation properties of ultrafiltration (UF) membranes.** **By controlling the aeration rate, injection frequency and the solution pH, membrane fouling was alleviated, especially under weakly acidic conditions. Additionally, owing to the higher rejection efficiency of the UF membrane, the effluent quality was improved, including the iron concentration, turbidity, and chromaticity.** This innovative separation method shows promising potential for application in removing heavy metals in water treatment.[ \[Art. #ARTNUM\]](#article-96074-2611225203)
* In this study, the use of an electrocoagulation-ultrafiltration (EC-UF) hybrid system for the treatment of mining impacted wastewater was investigated. A model wastewater solution containing copper, lead, cadmium and other constituents representative of mining impacted wastewater was used in this investigation. [\[Art. #ARTNUM\]](#article-96074-2082194095)
* Industrial wastewater is often contaminated with heavy metals and must undergo expensive and elaborate treatment. A new, environmentally friendly process, which allows both metals and water to be reused, has been developed. It comprises the following three process stages: firstly, a metal bonding agent (BA) is added to the wastewater to bind the heavy metal; secondly, the loaded BA is separated by ultrafiltration/microfiltration or a new hybrid process involving flotation and membrane filtration; and thirdly, the BA is regenerated. [\[Art. #ARTNUM\]](#article-96074-2050478705)
* **The complexation–ultrafiltration technique has been introduced as a capable system to remove heavy metals ions from wastewater.** This method needs a water-soluble polymer; therefore, in this paper we synthesized super water-soluble poly(itaconic acid) (PITA) and employed it in polymer-assisted ultrafiltration process to remove Pb(II) ions from synthetic wastewater solutions. [\[Art. #ARTNUM\]](#article-96074-2989198936)
* In-line addition of alum and ferric chloride was conducted at a hollow-fibre immersed ultrafiltration (UF) membrane pilot plant, using secondary effluent from a municipal wastewater treatment plant (WWTP) as the feed. The objective of such pretreatment was to remove phosphorus from the feed from an initial concentration of approximately 5 mg/L to below 0·3 mg/L. [\[Art. #ARTNUM\]](#article-96074-2151273409)
**Polymer enhanced ultrafiltration:**
* Some significant findings were reported by Juang and Shiau (2000), who studied the removal of Cu(II) and Zn(II) ions from synthetic wastewater using chitosan-enhanced membrane filtration. The amicon-generated cellulose YM10 was used as the ultrafilter. About 100% and 95% rejection were achieved at pH ranging from 8.5 to 9.5 for Cu(II) and Zn(II) ions, respectively. **The results indicated that chitosan significantly enhanced metals removal by 6–10 times compared to using membrane alone.** This could be attributed to the major role of the amino groups of chitosan chain, which served as coordination site for metal-binding. Polymer-supported ultrafiltration (PSU) technique has been shown recently to be a promising alternative for the removal of heavy metal ions from industrial effluent. This method employs proprietary water-soluble polymeric ligands to bind metal ions of interest, and the ultrafiltration technique to concentrate the formed macromolecular complexes and produce an effluent, essentially free of the targeted metal ions. [\[Art. #ARTNUM\]](#article-96074-2043219105)
* **In this work, a novel positively charged tight ultrafiltration (PCTUF) membrane was developed to remove heavy metal cations (Mn 2+ , Co 2+ , Ni 2+ , Zn 2+ and Cd 2+ ) from contaminated waters via electrostatic repulsion mechanism.** The results revealed that the prepared PCTUF membrane with its high perm-selectivity performance provides a worthy reference for highly efficient removal of heavy metal cations. [\[Art. #ARTNUM\]](#article-96074-2922823182)
* In this study, amine-terminated hyperbranched PAMAM (polyamidoamine) polymer (AT-HBP) was synthesized as a multifunctional chelating agent to remove two heavy metal ions (Cr(III) and Cu(II)) from the simulated wastewater solutions. Finally, hyperbranched dendritic polymer with lower expenses to synthesize compared to dendrimer underlined favorable properties as a multifunctional chelating agent and enhancement of ultrafiltration process for wastewater treatment.[\[Art. #ARTNUM\]](#article-96074-2921371567)
* In this study, aqueous solutions containing mixtures of heavy metals namely Zn (II), Pb (II), Cr (III), and Cr (VI) were treated by polymer-enhanced ultrafiltration (PEUF) using unmodified starch as binding biopolymer.[ \[Art. #ARTNUM\]](#article-96074-2134980036)
**Micellar enhanced ultrafiltration:**
* **Micellar-enhanced ultrafiltration(MEUF) is a powerful treatment process developed recently to remove heavy metals from wastewater,which combines ultrafiltration with surfactant technology.** Competitive adsorption of Cd2+,Zn2+,Pb2+ to SDS micelle micellar-enhanced ultrafiltration(MEUF) was studied for single solute and mixed solute containing cadmium ions,zinc ions and plumbum ions with sodium dodecyl sulfate(SDS) as surfactant. Results show that with the wastewater containing a variety of bivalence heavy metal ions, competitive adsorption to SDS micelle exists among various ions, and the sequence of competitive adsorption is Pb2+Zn2+Cd2+. [\[Art. #ARTNUM\]](#article-96074-2353167906)
* In this study micellar-enhanced ultrafiltration (MEUF) was used to simultaneously remove heavy metals from phosphorous rich drainage waters of a fertilizer company, obtaining the purification of the nutrient rich wastewater. [\[Art. #ARTNUM\]](#article-96074-2083344249)
Suppliers
| 4.1.1 | ultrafiltration |
|---|---|
| A positively charged tight UF membrane and its properties for removing trace metal cations via electrostatic repulsion mechanism | |
| Abstract The development of highly efficient membranes technology using low-pressure driven filtration process, is one of the principal challenges in the wastewater treatment field, especially those aimed at the removal of trace heavy metals. In this work, a novel positively charged tight ultrafiltration (PCTUF) membrane was developed to remove heavy metal cations (Mn 2+ , Co 2+ , Ni 2+ , Zn 2+ and Cd 2+ ) from contaminated waters via electrostatic repulsion mechanism. The PCTUF membrane was fabricated from a new polymer with poly (vinyl chloride co dimethylaminoethyl methacrylate), P (VC- co -DMA) via a nonsolvent induce phase separation (NIPS) process and following facile surface quaternization. The quaternization conditions, the pore structures and chemical properties of the membranes were investigated in detail. The optimally quaternized membrane possessed a positively charged surface and 3.27 nm charged channel with the water permeability of 84 L m −2 h −1 bar −1 . The rejections of heavy metal cations surpassed 95% for feed solutions containing 10 ppm heavy metal. Moreover, the influences of feed concentrations and the operating condition with pressure and pH on the membrane performances were also investigated. The results revealed that the prepared PCTUF membrane with its high perm-selectivity performance provides a worthy reference for highly efficient removal of heavy metal cations. | |
| 03/01/2019 00:00:00 | |
| Link to Article | |
| 4.1.2 | ultrafiltration |
| Adsorption of surfactant micelles and Cd2+/Zn2+ in micellar-enhanced ultrafiltration | |
| Abstract Micellar-enhanced ultrafiltration (MEUF) is a powerful treatment developed to remove heavy metals from wastewater. Efficient removal of Cd 2+ /Zn 2+ from wastewater was performed by MEUF using a polysulfone hollow ultrafiltration membrane, with sodium dodecyl sulfate (SDS) as the surfactant. The adsorption of surfactant micelles and Cd 2+ /Zn 2+ in MEUF was studied by changing the surfactant dosage and the Cd 2+ /Zn 2+ concentration in the feed. In addition, kinetics, adsorption isotherms, and thermodynamic rules were analyzed, and X-ray photoelectron spectroscopy (XPS) was conducted. It was found that when the Cd 2+ /Zn 2+ feed concentration was 50 mg/L, and the SDS dosage reached 2.15 g/L, the concentration of heavy metal ions in the permeate stabilized at around 1–4 mg/L, and the adsorption of Cd 2+ /Zn 2+ on SDS micelles followed second-order kinetics and the Langmuir isotherm laws. Adsorption is a spontaneous endothermic process in which the adsorption force is principally the attraction of opposite electrical charges. | |
| 11/01/2010 00:00:00 | |
| Link to Article | |
| 4.1.3 | ultrafiltration |
| Amine-terminated dendritic polymers as a multifunctional chelating agent for heavy metal ion removals | |
| In this study, amine-terminated hyperbranched PAMAM (polyamidoamine) polymer (AT-HBP) was synthesized as a multifunctional chelating agent to remove two heavy metal ions (Cr(III) and Cu(II)) from the simulated wastewater solutions. The AT-HBP was characterized by Fourier transformed infrared (FTIR), dynamic light scattering (DLS), and proton nuclear magnetic resonance (1H NMR) analysis. The removal process was carried out in two different methods, centrifuged process and ultrafiltration. The concentration of heavy metal ions before and after removal was measured by inductively coupled plasma (ICP) instrument. The removal processes were evaluated by changing different parameters such as solution pH, AT-HBP dosage, and metal ion concentration. To evaluate the extend of binding of heavy metal ions in the presence of AT-HBP the presence of salt in the solution was also examined on the performance of the removal system. The overall results indicated that removal percentages higher than 98% for Cr(III) and 86% for Cu(II) were achieved for heavy metal concentrations of 100 mg/L for both removal process methods. Furthermore, the function of second generation of polypropylenimine (PPI) was compared to AT-HBP. The results reveal that the removal of Cr(III) and Cu(II) ions by AT-HBP were approximately 20% and 10% higher compared to PPI, respectively. Finally, hyperbranched dendritic polymer with lower expenses to synthesize compared to dendrimer underlined favorable properties as a multifunctional chelating agent and enhancement of ultrafiltration process for wastewater treatment. | |
| 03/15/2019 00:00:00 | |
| Link to Article | |
| 4.1.4 | ultrafiltration |
| Ammonia removal from chicken manure digestate through vapor pressure membrane contactor (VPMC) and phytoremediation | |
| Abstract Ammonia removal from synthetic ammonia solutions and chicken manure digestate via vapor pressure membrane contactor through Polytetrafluoroethylene (PTFE) membrane was investigated. The highest ammonia mass flux, separation factor, and removal efficiencies of 28.6 ± 0.2 g N/m 2 h, 53.9 ± 10.7, and 97.6 ± 0.7% were observed for synthetic solutions, respectively. Ammonia removal efficiency of 93.6 ± 1.9% through membrane contactor was observed for chicken manure digestate decreasing the total ammonia concentration from 3643.5 ± 67.2 to 230.9 ± 46.2 mg N/L. Phytoremediation via Lemna minor species was used as a polishing step to remove remaining ammonia from the membrane contactor effluent. Total ammonia concentration was then decreased below 2 mg N/L through evaporation, nitrification, and plant uptake processes occurring in the phytoremediation containers. This study reveals that ammonia can be successfully removed via VPMC and phytoremediation systems and the process is implementable as it can be coupled to anaerobic digestion processes to recover ammonia and to prevent ammonia inhibition. | |
| 02/01/2019 00:00:00 | |
| Link to Article | |
| 4.1.5 | ultrafiltration |
| Application of Ultrafiltration Membrane Technology in Pulp and Paper Mills in Indian Context: A Review | |
| In general, Indian pulp and paper mills generate 25-225 m³ wastewater/tonne of paper. Pulp and paper mill effluent carries high pollution load in terms of COD, BOD, absorbable organic halides (AOX) and is dark brown in colour mainly due to the lignin and lignin derivatives. Stringent application of new environmental norms in the form of CREP (Corporate Responsibility for Environmental Protection) has forced many mills to close down their operation. Hence, large proportion of water now being discharged need to be recycled back into the system at the appropriate intake points with/without treatment. There are several conventional treatment processes employed in Indian paper industry which effectively remove BOD, TSS, and also COD but do not remove colour, AOX, heavy metal and process chemicals as per the desired level to recirculate the process water in good condition. Membrane technology is being adopted increasingly in the paper mills for closing their mill production process. Application of membrane technology is one such option which can improve the recycled water quality by removal of heavy metal contaminates, COD, TSS, colour, AOX, and lignin. This shall reduce the load on conventional recovery evaporation system with no significant loss of inorganic compounds. Membranes also provide an effective method of closing the chelating stages and allow the filtrates to be used as bleach plant wash liquors. Membrane filtration also allows efficient recycling of white water. The present paper reviews current status of ultrafiltration in terms of R&D efforts and its application to the paper industry with due focus of system closure in Indian pulp and paper mills. | |
| 01/01/2009 00:00:00 | |
| Link to Article | |
| 4.1.6 | ultrafiltration |
| Biosorption of Heavy Metal by Algae Biomass in Surface Water | |
| Discharging wastewater containing heavy metals of Cu, Pb, Zn and Cd into water bodies can cause toxicity in plants and aquatic animals and some of them will be unable to survive except algae. Wastewater treatment method to remove heavy metal contaminants includes chemical precipitation, ion exchange, membrane, filtration, adsorption using activated carbon. However, these methods are either expensive or have other disadvantages such as high energy consumption and inefficiencies when existing heavy metals are at trace concentration. Biosorption using algae biomass can be an alternative method to eliminate heavy metals. The objective of the project is to investigate the capability of Marine Algae (MA) and Freshwater Algae (FA) bi-omass in adsorbing heavy metals of Cu, Pb, Zn and Cd from water medium using synthetic water and industrial water. MA and FA were obtained from the eastern coast of Pulau Ubin and local fish farm respectively. After being fully washed with deionised water, dried in a furnace for 105°C, they are grinded to pass 1 mm2 of siever. MA and FA were characterised using FTIR to determine their functional groups. An industrial water was collected from industrial discharge from metal fac-tories in northern side of Singapore. Effect of adsorption time, adsorbent concentra-tion, and pH were studied. The result showed that FA and MA had a higher capability in adsorbing a total metal of about 40 ppm level from an industrial water, or 4 times than synthetic water concentration, at the same adsorbent dosage of 50 mg. In con-clusion, the presence of various functional groups, hydroxyl, carboxylic and amine groups, in all MA and FA samples had enabled the algae biomass to adsorb heavy metals of Cu, Pb, Cd and Zn from synthetic and industrial water. Due to their bio-sorptive properties and fast adsorption capability, algae could be a potential method for cleaning up surface water or post-treatment of wastewater and minimise the cost of eutrophication. | |
| 01/01/2016 00:00:00 | |
| Link to Article | |
| 4.1.7 | ultrafiltration |
| Competitive adsorption of Cd~(2+),Zn~(2+),Pb~(2+) to SDS micelle in micellar-enhanced ultrafiltration | |
| Micellar-enhanced ultrafiltration(MEUF) is a powerful treatment process developed recently to remove heavy metals from wastewater,which combines ultrafiltration with surfactant technology.Competitive adsorption of Cd2+,Zn2+,Pb2+ to SDS micelle micellar-enhanced ultrafiltration(MEUF) was studied for single solute and mixed solute containing cadmium ions,zinc ions and plumbum ions with sodium dodecyl sulfate(SDS) as surfactant.Results show that with the wastewater containing a variety of bivalence heavy metal ions,competitive adsorption to SDS micelle exists among various ions,and the sequence of competitive adsorption is Pb2+Zn2+Cd2+. The experiment has clarified the cooperative adsorption relation of Cd-Zn and the resistant adsorption relation of Zn-Pb. | |
| 01/01/2008 00:00:00 | |
| Link to Article | |
| 4.1.8 | ultrafiltration |
| Enhanced ammonia recovery from wastewater by Nafion membrane with highly porous honeycomb nanostructure and its mechanism in membrane distillation | |
| Abstract Removing nitrogen from wastewater by conventional treatment methods requires substantial energy, only to release it back to the atmosphere as gaseous nitrogen. Herein, we investigated the applicability of membrane distillation (MD) in resource recovery from sludge digestate by controlling the volatility and pressure of the vapor transport across the membrane to concentrate ammonia in the permeate stream. A mixture of Nafion ionomer and Multiwall Carbon Nanotubes (MWCNTs) were incorporated into a Poly (vinylidene fluoride-co-hexafluoropropene; PVDF-HFP) nanofiber matrix to fabricate a nanoporous honeycomb Nafion membrane featuring high recovery and increased mechanical strength. Theoretical modeling was conducted to predict the expected performance of the fabricated Nafion membrane under different operation conditions and to reveal the mechanism behind the enhanced recovery of Nafion membranes in the MD process. The resultant Nafion (8%)/MWCNT (2.5%)/PVDF-HFP nanofibrous membrane showed up to three times higher ammonia recovery compared to the commercial PVDF membrane from a feed with an ammonia concentration of 300 mg/L. The theoretical analysis quantitatively revealed that the Nafion containing membrane can not only suppress the negative effect of membrane's structural resistance on the ammonia recovery efficiency but also enhance the efficiency. In addition, we also uncovered that the effect of Nafion on ammonia recovery efficiency was maximized when the Nafion 8% membrane was employed. This study demonstrated an innovative and realistically applicable MD treatment process for recovering resource, which integrates low-grade heat and has scaling-up potential for wastewater treatment plants. | |
| 07/01/2019 00:00:00 | |
| Link to Article | |
| 4.1.9 | ultrafiltration |
| Hybrid membrane systems for secondary effluent polishing for unrestricted reuse for agricultural irrigation | |
| Field experiments are in progress for secondary wastewater upgrading for unrestricted utilization for agricultural irrigation. The integrative approach of secondary effluent polishing is based on using a hybrid UltraFiltration (UF) and Reverse Osmosis (RO) membrane pilot system with a capacity of around 1 m3/hr. The UF effluent is used to feed the RO membranes. The RO permeate is subsequently applied for vegetable irrigation. Field results indicate the importance of the UF component in the removal of the organic matter and the pathogens that are still contained in the secondary effluent. Under specific conditions, when the dissolved solids content is relatively low, regarding sanitary and health aspects, the UF effluent can be applied for unrestricted irrigation. During the RO stage most nutrients are removed, allowing application of the effluent without jeopardizing the soil fertility and the aquifers. Preliminary economic assessment indicates that the extra cost for effluent polishing via the UF stage only is in the range of 5 to 15 US cents/m 3 . The extra cost for the RO stage is also assessed at 10 to 25 US cents/m 3 . The additional cost depends to a large extent on the quality of the incoming raw secondary effluent and local requirements of the command region. | |
| 09/01/2004 00:00:00 | |
| Link to Article | |
| 4.1.10 | ultrafiltration |
| Methods of Removing Heavy Metals from Industrial Wastewater | |
| Methods for treating industrial wastewater containing heavy metals often involve technologies for reduction of toxicity in order to meet technology-based treatment standards. This article was focused on the recently developed and newly applicable various treatment processes for the removal of heavy metals from industrial wastewater. Physico-chemical removal processes such as; adsorption on new adsorbents, ion exchange, membrane filtration, electrodialysis, reverse osmosis, ultrafiltration and photocatalysis were discussed. Their advantages and drawbacks in application were evaluated. In the processes of biological treatments microorganisms play a role of settling solids in the solution. Activated sludge, trickling filters, stabilization ponds are widely used for treating industrial wastewater. Bioadsorption is a new biological method and various low cost bioadsorbents (agricultural waste, forest waste, industrial waste, algae etc.) are used for maximum removal of heavy metals from wastewater. Bioadsorption techniques are eco friendly best solutions for removing heavy metals from wastewater rather than physic-chemical methods. But chemical methods are most suitable treatments for toxic inorganic compounds produced from various industries which cannot removed from any biological and physical techniques. Keywords—heavy metals; removal techniques; | |
| 01/01/2015 00:00:00 | |
| Link to Article | |
| 4.1.11 | ultrafiltration |
| New trends in removing heavy metals from industrial wastewater | |
| Abstract Innovative processes for treating industrial wastewater containing heavy metals often involve technologies for reduction of toxicity in order to meet technology-based treatment standards. This article reviews the recent developments and technical applicability of various treatments for the removal of heavy metals from industrial wastewater. A particular focus is given to innovative physico-chemical removal processes such as; adsorption on new adsorbents, membrane filtration, electrodialysis, and photocatalysis. Their advantages and limitations in application are evaluated. The main operating conditions such as pH and treatment performance are presented. Published studies of 94 cited references (1999–2008) are reviewed. It is evident from survey that new adsorbents and membrane filtration are the most frequently studied and widely applied for the treatment of metal-contaminated wastewater. However, in the near future, the most promising methods to treat such complex systems will be the photocatalytic ones which consume cheap photons from the UV-near visible region. They induce both degradation of organic pollutants and recovery of metals in one-pot systems. On the other hand, from the conventional processes, lime precipitation has been found as one of the most effective means to treat inorganic effluent with a metal concentration of >1000 mg/L. It is important to note that the overall treatment cost of metal-contaminated water varies, depending on the process employed and the local conditions. In general, the technical applicability, plant simplicity and cost-effectiveness are the key factors in selecting the most suitable treatment for inorganic effluent | |
| 10/01/2011 00:00:00 | |
| Link to Article | |
| 4.1.12 | ultrafiltration |
| Optimization of phosphorus removal in secondary effluent using immersed ultrafiltration membranes with in-line coagulant pretreatment — implications for advanced water treatment and reuse applications | |
| In-line addition of alum and ferric chloride was conducted at a hollow-fibre immersed ultrafiltration (UF) membrane pilot plant, using secondary effluent from a municipal wastewater treatment plant (WWTP) as the feed. The objective of such pretreatment was to remove phosphorus from the feed from an initial concentration of approximately 5 mg/L to below 0·3 mg/L. The simplified in-line coagulant addition process involved hydraulic mixing of the coagulant into the feed and subsequent flocculation, and a greatly reduced (12 – 14 min) flocculation time relative to conventional coagulation-flocculation-settling treatment. Both alum and ferric chloride effectively removed phosphorus to below the 0·3 mg/L threshold when applied as a pretreatment at optimized doses, both of which were below the WWTP’s current coagulant dose (as ferrous chloride). This simplified pre-treatment scheme provided consistent enhanced removal of phosphorus and organic compounds. These results suggest that simplified in-line coagul... | |
| 11/01/2013 00:00:00 | |
| Link to Article | |
| 4.1.13 | ultrafiltration |
| Poly(itaconic acid)-assisted ultrafiltration of heavy metal ions’ removal from wastewater | |
| The complexation–ultrafiltration technique has been introduced as a capable system to remove heavy metals ions from wastewater. This method needs a water-soluble polymer; therefore, in this paper we synthesized super water-soluble poly(itaconic acid) (PITA) and employed it in polymer-assisted ultrafiltration process to remove Pb(II) ions from synthetic wastewater solutions. The itaconic acid can be produced from different agricultural products and is a green and eco-friendly material. Factors influencing the removal of the metals ions including poly(itaconic acid) concentration, pH and permeate flux were investigated. The results showed that the maximum percentage of metal ion removal was obtained in the basic pH (pH > 7). The flux test was performed by 200 mg/L of poly(itaconic acid) and after 60 min, the flux of membrane was 33.4 L/m2h. The simultaneously selective removal ability of the poly(itaconic acid) for adsorption of different metal ions (Pb2+, Sn2+, Cu2+, Zn2+, and Cd2+) was also studied. The trend of rejection was Pb2+ > Cu2+ > Sn2+ > Zn2+ > Cd2+. The highest rejection of Pb(II) ions was achieved as 86%. Generally, the results of this research demonstrated that poly(itaconic acid) (with two carboxyl groups on its repeating unit) is more effective in removing heavy metals ions from wastewater in comparison with customary polymers. | |
| 12/01/2019 00:00:00 | |
| Link to Article | |
| 4.1.14 | ultrafiltration |
| Removal of Heavy Metal from Wastewater Using Ion Exchange Membranes | |
| Clean water supplies are vital for industry, agriculture, and energy production. However, the water pollution issue is becoming more serious due to ever-increasing wastewater discharges from the industries into the environment. As the freshwater resource is limited, it is extremely crucial to reuse the wastewater after it has been treated to remove the heavy metal ions and other organic pollutants, which is believed to be the only way to find the new water resource. In view of the significance of treatment of wastewater contaminants, various remediation technologies are proposed and developed for efficient removal of heavy metal ions, including ultrafiltration, nanofiltration, reverse osmosis, forward osmosis, adsorption, electrodialysis method, and fuel cell method. This chapter starts with a brief introduction of heavy metals, which are chromium, nickel, copper, zinc, cadmium, mercury, and lead. Then both physical treatment and chemical treatment are summarized. Finally, the remaining challenges and future perspectives are highlighted. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
| 4.1.15 | ultrafiltration |
| Removal of heavy metal ions from mixed solutions via polymer‐enhanced ultrafiltration using starch as a water‐soluble biopolymer | |
| In this study, aqueous solutions containing mixtures of heavy metals namely Zn (II), Pb (II), Cr (III), and Cr (VI) were treated by polymer-enhanced ultrafiltration (PEUF) using unmodified starch as binding biopolymer. The performance of starch in removing these heavy metals was compared with that of polyethylene glycol (PEG) a commonly used polymer in PEUF processes. Rejection coefficients and flux were studied under different values of pH solution and metal ion concentrations maintaining the transmembrane pressure constant at 1.5 bar. At pH 7, and starch concentration of 0.05%, the rejection was the highest at around 90%. As metal ion concentration increased from 10 to 50 mg/L, the rejection of metal ions decreased. It was found that starch gave higher rejection for Zn (II) and Cr (III) at 0.05 g/L of polymer concentration, whereas 1 g/L of PEG concentration gave higher rejection for Cr (VI) at 10 mg/L. The influence of metal ion concentration on Pb (II) rejection is not significant for the two selected polymers. The rejection of these metal ions by starch in this study is found to be influenced by granule structure that generally behaved in a nonionic manner. V C 2014 American Institute of Chemical Engineers Environ Prog, 00: 000‐000, 2014 | |
| 03/04/2015 00:00:00 | |
| Link to Article | |
| 4.1.16 | ultrafiltration |
| Removal of heavy metals from mining impacted water by an electrocoagulation-ultrafiltration hybrid process | |
| In this study, the use of an electrocoagulation-ultrafiltration (EC-UF) hybrid system for the treatment of mining impacted wastewater was investigated. A model wastewater solution containing copper, lead, cadmium and other constituents representative of mining impacted wastewater was used in this investigation. The effects of key operational parameters including electrolysis time, current density, and solution pH on the performance of the EC and EC-UF systems were systematically investigated. The removal rates of copper and lead by the EC process were consistently higher than that of cadmium. It is probable that the removal mechanism of cadmium was different from that of the base metal copper and lead. Results reported here indicate that an EC-UF hybrid system could be very effective in removing heavy metals at high solution pH. At an acidic condition, the removal efficiency of heavy metal by both EC and UF reduced dramatically. However, the overall removal efficiency by the hybrid EC-UF system remained q... | |
| 11/01/2009 00:00:00 | |
| Link to Article | |
| 4.1.17 | ultrafiltration |
| Selective Separation of Heavy Metals from Industrial Wastewater Streams by Means of Heavy Metal Bonding Agents | |
| Industrial wastewater is often contaminated with heavy metals and must undergo expensive and elaborate treatment. A new, environmentally friendly process, which allows both metals and water to be reused, has been developed. It comprises the following three process stages: firstly, a metal bonding agent (BA) is added to the wastewater to bind the heavy metal; secondly, the loaded BA is separated by ultrafiltration/microfiltration or a new hybrid process involving flotation and membrane filtration; and thirdly, the BA is regenerated. The first results from the characterisation of selected BAs (synthetic hydrotalcites and synthetic zeolites) in terms of their bonding kinetics, maximum loading capacity and regeneration potential are presented. | |
| 10/01/2004 00:00:00 | |
| Link to Article | |
| 4.1.18 | ultrafiltration |
| Simultaneous removal of heavy metals from phosphorous rich real wastewaters by micellar-enhanced ultrafiltration | |
| Abstract In this study micellar-enhanced ultrafiltration (MEUF) was used to simultaneously remove heavy metals from phosphorous rich drainage waters of a fertilizer company, obtaining the purification of the nutrient rich wastewater. Response surface methodology approach was used to model and optimise the rejection coefficients of cadmium and copper. The factors studied were pH and SDS feed concentration. Results show that the removal of copper and cadmium was more efficient at low pH values. SDS feed concentration higher than 60 mM was needed to obtain an efficient removal of cadmium and copper due to the competition of other metals present in the real drainage waters. The optimum rejection coefficients achieved were 84.3% and 75.0% for cadmium and copper, respectively, at the pH value of 3.2 and SDS feed concentration of 75.6 mM. In addition, calculated rejection coefficients for zinc and nickel show that copper was the least trapped heavy metal and the MEUF removal efficiency was as follows, Zn = Ni > Cd > Cu. The flux decreased when increasing SDS feed concentration due to concentration polarisation, which was more significant above the SDS feed concentration of 60 mM. Irreversible fouling was negligible in the whole set of experiments. Secondary pollution due to the SDS leakage to the permeate was also negligible. | |
| 03/01/2012 00:00:00 | |
| Link to Article | |
| 4.1.19 | ultrafiltration |
| Synergistic process using Fe hydrolytic flocs and ultrafiltration membrane for enhanced antimony(V) removal | |
| Abstract Antimony (Sb) is harmful to human health, and Sb(V) is much more difficult to remove from water than other toxic elements such as arsenic (As). Theoretical studies have suggested that in situ flocs have stronger adsorption ability toward heavy metals than pre-made adsorbents. We believe that rational design of in situ flocs and the associated device structure will enable a floc-based device to be utilized in the removal of heavy metals. Based on this concept, we developed an integrated process taking advantage of the strong adsorption abilities of in-situ Al or Fe hydrolytic flocs and excellent separation properties of ultrafiltration (UF) membranes. We found that flocs could be well dispersed in a membrane tank with aeration from the bottom, and Fe-based flocs performed better in removing Sb(V) and alleviating membrane fouling than Al-based flocs. We also demonstrated that higher Sb(V) removal efficiency was induced with continuous injection, and lower solution pH. By controlling the aeration rate, injection frequency and the solution pH, membrane fouling was alleviated, especially under weakly acidic conditions. Additionally, owing to the higher rejection efficiency of the UF membrane, the effluent quality was improved, including the iron concentration, turbidity, and chromaticity. This innovative separation method shows promising potential for application in removing heavy metals in water treatment. | |
| 09/01/2017 00:00:00 | |
| Link to Article | |
| 4.1.20 | ultrafiltration |
| The advantages of microfiltration/ultrafiltration membrane combined with conventional water treatment process and application examples | |
| The microfiltration(MF)/ultrafiltration(UF)membrane combined process has been widely applied in the field of water treatment.Combined with conventional water treatment process,such as adsorption,precipitation,flocculation and coprecipitation,MF/UF membrane could achieve the satisfactory results which couldn't be obtained by using conventional water treatment process alone.The MF/UF combined process could remove effectively heavy metals,radioactive materials,fluoride and most of the pollutants in backwashing wastewater or reverse osmosis concentrate.This review focused on the removal of specific pollutants from water with MF/UF membrane combined process.The advantages and the future research needs for the MF/UF membrane combined process are also discussed. | |
| 01/01/2013 00:00:00 | |
| Link to Article | |
| 4.1.21 | ultrafiltration |
| The Nanomembrane Toilet: Membranes for water recovery in decentralised sanitation systems | |
| Poster presented at the Cranfield Doctoral Network Annual Event 2018.In this research, the Nanomembrane Toilet is introduced as a single household sanitation system independent of grid produced power. To address paucity of information on super-concentrated wastewater characterisation, chemical oxygen demand (COD), ammoniacal nitrogen, and E.Coli bacteria are analysed in the wastewater storage tank. A small-scale combustor is developed (Onabanjo et al., 2016) to operate on the faecal sludge phase, producing low-grade heat that is used to provide the vapour pressure gradient for thermally-driven membrane separation of water from faecally contaminated urine (FCU). Subsequently, a membrane technology is developed that can provide a single-stage treatment process, separating clean water from FCU. In this study, the impact of temperature on water recovery from FCU (urine:faece 56:1) by membranes (PTFE, nominal pore size 0.1 µm) is investigated. Out of 40, 50, and 60 ⁰C operational temperature values, operation at 60 c is shown to enable the process for the removal of organics, inorganics, and pathogens, sufficient to meet the ISO/PC 305 standard for sustainable non-sewered sanitation systems (American National Standards Institute, 2016). Furthermore, influence of faecal concentration in the FCU (at optimised temperature of 60 ⁰C) on the produced water quality is studied. The results show that high faecal concentration leads to high ammonium formation in the feed, hence faster ammonia breakthrough is observed. Lastly, the membrane pore size was optimised for the treatment of FCU at constant faecal concentration and temperature. It is concluded that only 0.1 µm membrane pore size is capable of removing ammonia, COD, and E.Coli to the proposed ISO standard at both 40 and 60 ⁰C. Importantly, this study has demonstrated that through integration of this modularised componentry into the Nanomembrane Toilet, single household sanitation can be delivered, independent of external power sources and infrastructure. | |
| 10/22/2018 00:00:00 | |
| Link to Article | |
4.2 nanofiltration (NF)
Nanofiltration is a membrane filtration-based method that uses nanometer sized through-pores that pass through the membrane. Nanofiltration membranes have pore sizes from 1-10 nanometers, smaller than that used in microfiltration and ultrafiltration, but just larger than that in reverse osmosis.[\[Wiki\]](https://en.wikipedia.org/wiki/Nanofiltration#:\~:text=Nanofiltration%20is%20a%20membrane%20filtration,than%20that%20in%20reverse%20osmosis.)
**Highlights:**
* NF is capable of removing ions that contribute significantly to the osmotic pressure hence allows operation pressures that are lower than those RO. For NF to be effective pre-treatment is needed for some heavily polluted waters; Membranes are sensitive to free chlorine. Soluble elements cannot be separated from water. Xu and others reported NF membrane for textile wastewater treatment, the prepared membrane displayed good removal of heavy metal ions, common salts and dyes, showing high removal efficiency toward metal ions and cationic dyes. [\[Paper\]](https://www.intechopen.com/books/wastewater-and-water-quality/wastewater-treatment-using-membrane-technology)
* In order to effectively separate chloride (such as NaCl) and sulfate (such as Na2SO4 ) for high saline wastewater recycling, one commercial NF membrane (named Desal-DL) was employed in the permeation of the single and binary salt solutions of NaCl and Na 2 SO 4 with a lab-scale cross-flow batch module, where the salt concentration ranged from 4 to 96 g L1 and the operating pressures varied from 0.6 to 2.4 MPa as well as the temperature was kept under room temperature. The experimental results showed that the Desal-DL NF membrane had a low rejection to NaCl and a high rejection to Na2SO4 for single salt solutions. [\[Art. #ARTNUM\]](#article-96121-2324824251)
* The focus of this research is to study the potential of nanofiltration membrane technology in removing ammonia–nitrogen from the aquaculture system. [\[Art. #ARTNUM\]](#article-96121-2126264117)
**(Nano)Composite membranes:**
* One must **separate phosphorus from the heavy metals in order to produce fertilizers of high quality.** Among various available methods, nanofiltration (NF) has been demonstrated to be a feasible and promising option when the sewage sludge undergoes acidic dissolution and the operating pH is around 2. Because the performance of commercially available thin film composite (TFC) NF membranes reported thus far has great room for improvement, the development of highly permeable positively charged NF membranes is recommended. To this aim, a NF membrane that is desirable for phosphorus recovery was fabricated via interfacial polymerization of polyethylenimine (PEI) and trimesoyl chloride (TMC) on a porous poly(ether sulfone) (PES) membrane substrate.[ \[Art. #ARTNUM\]](#article-96121-2510602979)
* This is a report of the first attempt to develop a **composite NF membrane comprising a molecularly designed pentablock copolymer selective layer for the removal of heavy metal ions.** The resultant NF membrane has a mean effective pore diameter of 0.50 nm, a molecular weight cutoff of 255 Da, and a reasonably high pure water permeability (A) of 2.4 LMH/bar. The newly developed NF membrane can effectively remove heavy metal cations such as Pb2+, Cd2+, Zn2+, and Ni2+ with a rejection of >98.0%.[ \[Art. #ARTNUM\]](#article-96121-2314982393)
* For the first time, thin film nanocomposite (TFN) nanofiltration membranes incorporated with graphene oxide (GO) were synthesized and used to separate phosphorus from water source of different properties. [\[Art. #ARTNUM\]](#article-96121-2767186783)
**Commercial membranes:**
* Nanofiltration (NF) and reverse osmosis (RO) membranes might be used to recover the nutrients from anaerobically treated black water. The permeate might be used in a water reuse scheme. The focus of this paper is to test commercially available NF and RO membranes to remove nutrients from anaerobically treated black water in order to meet the Dutch guidelines. A large number of commercial tubular, capillary and flat sheet NF and RO membranes was tested on laboratory scale on their performance to meet the Dutch guidelines for ammonium and phosphate. The ammonium and phosphate concentrations used were based on the effluent composition of anaerobically treated black water. Ammonium and phosphate rejection were both measured in synthetic single salt and multi-ion mixtures and in anaerobic effluent. **The rejection for ammonium (30-95%) is neither sufficient for discharge nor potable water use. The rejection of phosphate (74-99%) is in most cases almost sufficient to meet the standards for potable water.** [\[Art. #ARTNUM\]](#article-96121-2000756297)
* Nanofiltration tests were carried out on four different commercial membranes: NF97, NF99, NF99H, and NF90. Among these, **all membranes removed chloride but only NF97 and NF90 were able to remove nitrate in compliance with Chilean drinking water standard**, showing rejections of 97% and 87%, respectively, in an optimum pressure range of 12–20 bar in which the NF90 produced 3.5 times more permeated water than NF97. [\[Art. #ARTNUM\]](#article-96121-3012167332)
* The fractionation of nitrogen (as ammonia/ammonium) and phosphorus (as phosphate ions) present in the dairy manure digestate was investigated using a nanofiltration membrane NF270. The filtration and separation efficiencies were correlated to pH across the range 3 4 –P was achieved by series of diafiltration (DF) operations which further separated the nitrogen. The separation of nutrients benefited from an advantageous membrane process with potential added value for a wide range of industries. The analysis of the process economics for a membrane based plant illustrates that the recovery of nutrients, particularly NH3 –N, may be commercially feasible when compared to manufactured anhydrous NH3 . [\[Art. #ARTNUM\]](#article-96121-213046232)
Suppliers
| 4.2.1 | nanofiltration (NF) |
|---|---|
| An L-cystine/L-cysteine impregnated nanofiltration membrane with the superior performance of an anchoring heavy metal in wastewater | |
| Considerable efforts are being made to develop new materials and technologies for the efficient and fast removal of toxic ions in drinking water. In this work, we developed a sulfur-complexed strategy to enhance the removal capability of heavy metal ions using the polyamide nanofiltration membrane by the covalent anchoring of L-cystine and L-cysteine. The sulfur-functionalized polyamide nanofiltration membrane exhibits superior complexation of heavy metal ions and can efficiently remove them from high-concentration wastewater. As a result, the sulfur-functionalized nanofiltration membrane not only showed excellent desalination performance but also achieved a record removal rate of heavy metal ions (99.99%), which can effectively reduce Hg(II) concentration from 10 ppm to an extremely low level of 0.18 ppb, well below the acceptable limits in drinking water (2 ppb). Moreover, the sulfur-functionalized nanofiltration membrane showed an exciting long-term stability and can be easily regenerated without significant loss of Hg(II) removal efficiency even after six cycles. Such outstanding performances were attributed to the synthetic effect of Hg–S coordinative interaction, electrostatic repulsion, and the sieving action of nanopores. These results highlight the tremendous potential of thiol/disulfide-functionalized NF active layer as an appealing platform for removing heavy metal ions from polluted water with high performance in environmental remediation. | |
| 01/01/2020 00:00:00 | |
| Link to Article | |
| 4.2.2 | nanofiltration (NF) |
| Comparative study of nanofiltration and ion exchange for nitrate reduction in the presence of chloride and iron in groundwater. | |
| Abstract Public concern on the groundwater contamination by nitrate has grown significantly in recent years. The objective of this study was to determine the appropriate treatment to reduce the nitrate content in the presence of other ions from groundwater, for which nanofiltration and ion exchange were evaluated. In nanofiltration, the effects of pressure, feed flow, initial composition, and performance were studied, in ion exchange the flow rate, initial composition, and resin regeneration process. Nanofiltration tests were carried out on four different commercial membranes: NF97, NF99, NF99H, and NF90. Among these, all membranes removed chloride but only NF97 and NF90 were able to remove nitrate in compliance with Chilean drinking water standard, showing rejections of 97% and 87%, respectively, in an optimum pressure range of 12–20 bar in which the NF90 produced 3.5 times more permeated water than NF97. For ion exchange tests, Purolite A520E resin was used, which decreased nitrate content to Due to the ability to remove both nitrate and chloride, and being able to remove iron if necessary, nanofiltration was chosen as the appropriate treatment. | |
| 03/09/2020 00:00:00 | |
| Link to Article | |
| 4.2.3 | nanofiltration (NF) |
| Comparison of the behavior of two nanofiltration membranes for sweet whey demineralization | |
| Abstract Nanofiltration is a process used to separate mineral salts from lactose, having previously removed the proteins by ultrafiltration. Both proteins and lactose can be used as raw materials to prepare a variety of products. In this paper, we studied the feasibility of demineralizing sweet whey obtained from the cheese industry of the Comunidad Valenciana (Spain) using membrane technologies. The NF200 membrane showed the highest volumetric flux and solute rejection values, whereas the DS-5 DL membrane showed the lowest values. The volumetric fluxes obtained with the NF200 and DS-5 DL membranes in these experiments with the ultra-filtered whey demonstrated significant differences between membranes. Concerning solute rejection, the highest values were obtained using the NF200 membrane. The chosen parameter to evaluate the demineralization capability was solute flux. In this way, the values obtained for chloride ion were 9.90 and 32.42 g/ (m 2 ·h) for the NF200 and DS-5 DL membranes, respectively, with the highest demineralization rates being achieved with the DS-5 DL membrane. | |
| 03/01/2007 00:00:00 | |
| Link to Article | |
| 4.2.4 | nanofiltration (NF) |
| Molecular Design of Nanofiltration Membranes for the Recovery of Phosphorus from Sewage Sludge | |
| With the rapid depletion of mineral phosphorus, the recovery of phosphorus from sewage sludge becomes increasingly important. However, the presence of various contaminants such as heavy metals in sewage sludge complicates the issue. One must separate phosphorus from the heavy metals in order to produce fertilizers of high quality. Among various available methods, nanofiltration (NF) has been demonstrated to be a feasible and promising option when the sewage sludge undergoes acidic dissolution and the operating pH is around 2. Because the performance of commercially available thin film composite (TFC) NF membranes reported thus far has great room for improvement, the development of highly permeable positively charged NF membranes is recommended. To this aim, a NF membrane that is desirable for phosphorus recovery was fabricated via interfacial polymerization of polyethylenimine (PEI) and trimesoyl chloride (TMC) on a porous poly(ether sulfone) (PES) membrane substrate. Through an optimization of the interf... | |
| 10/03/2016 00:00:00 | |
| Link to Article | |
| 4.2.5 | nanofiltration (NF) |
| Moving towards sustainable resources: Recovery and fractionation of nutrients from dairy manure digestate using membranes | |
| Abstract The fractionation of nitrogen (as ammonia/ammonium) and phosphorus (as phosphate ions) present in the dairy manure digestate was investigated using a nanofiltration membrane NF270. The filtration and separation efficiencies were correlated to pH across the range 3 4 –P was achieved by series of diafiltration (DF) operations which further separated the nitrogen. The separation of nutrients benefited from an advantageous membrane process with potential added value for a wide range of industries. The analysis of the process economics for a membrane based plant illustrates that the recovery of nutrients, particularly NH 3 –N, may be commercially feasible when compared to manufactured anhydrous NH 3 . | |
| 09/01/2015 00:00:00 | |
| Link to Article | |
| 4.2.6 | nanofiltration (NF) |
| New trends in removing heavy metals from industrial wastewater | |
| Abstract Innovative processes for treating industrial wastewater containing heavy metals often involve technologies for reduction of toxicity in order to meet technology-based treatment standards. This article reviews the recent developments and technical applicability of various treatments for the removal of heavy metals from industrial wastewater. A particular focus is given to innovative physico-chemical removal processes such as; adsorption on new adsorbents, membrane filtration, electrodialysis, and photocatalysis. Their advantages and limitations in application are evaluated. The main operating conditions such as pH and treatment performance are presented. Published studies of 94 cited references (1999–2008) are reviewed. It is evident from survey that new adsorbents and membrane filtration are the most frequently studied and widely applied for the treatment of metal-contaminated wastewater. However, in the near future, the most promising methods to treat such complex systems will be the photocatalytic ones which consume cheap photons from the UV-near visible region. They induce both degradation of organic pollutants and recovery of metals in one-pot systems. On the other hand, from the conventional processes, lime precipitation has been found as one of the most effective means to treat inorganic effluent with a metal concentration of >1000 mg/L. It is important to note that the overall treatment cost of metal-contaminated water varies, depending on the process employed and the local conditions. In general, the technical applicability, plant simplicity and cost-effectiveness are the key factors in selecting the most suitable treatment for inorganic effluent | |
| 10/01/2011 00:00:00 | |
| Link to Article | |
| 4.2.7 | nanofiltration (NF) |
| Novel Nanofiltration Membranes Consisting of a Sulfonated Pentablock Copolymer Rejection Layer for Heavy Metal Removal | |
| Facing stringent regulations on wastewater discharge containing heavy metal ions, various industries are demanding more efficient and effective treatment methods. Among the methods available, nanofiltration (NF) is a feasible and promising option. However, the development of new membrane materials is constantly required for the advancement of this technology. This is a report of the first attempt to develop a composite NF membrane comprising a molecularly designed pentablock copolymer selective layer for the removal of heavy metal ions. The resultant NF membrane has a mean effective pore diameter of 0.50 nm, a molecular weight cutoff of 255 Da, and a reasonably high pure water permeability (A) of 2.4 LMH/bar. The newly developed NF membrane can effectively remove heavy metal cations such as Pb2+, Cd2+, Zn2+, and Ni2+ with a rejection of >98.0%. On the other hand, the membrane also shows reasonably high rejections toward anions such as HAsO42– (99.9%) and HCrO4– (92.3%). This performance can be attributed ... | |
| 12/02/2014 00:00:00 | |
| Link to Article | |
| 4.2.8 | nanofiltration (NF) |
| Nutrient removal by NF and RO membranes in a decentralized sanitation system | |
| Decentralized treatment of domestic wastewater offers the possibility of water and nutrient reuse. In a decentralized sanitation system the household wastewater streams are separated in a large diluted stream (gray water) and a small and concentrated stream (black water) containing important nutrients like ammonium and phosphate. Nanofiltration (NF) and reverse osmosis (RO) membranes might be used to recover the nutrients from anaerobically treated black water. The permeate might be used in a water reuse scheme. In case of water reuse the produced permeate should meet guidelines for potable water or meet new guidelines which might be applied in the future for intermediate quality of water, for example toilet flushwater; when this is not possible the permeate should meet guidelines for discharge. The most stringent guidelines apply for ammonium and phosphate. The focus of this paper is to test commercially available NF and RO membranes to remove nutrients from anaerobically treated black water in order to meet the Dutch guidelines. A large number of commercial tubular, capillary and flat sheet NF and RO membranes was tested on laboratory scale on their performance to meet the Dutch guidelines for ammonium and phosphate. The ammonium and phosphate concentrations used were based on the effluent composition of anaerobically treated black water. Ammonium and phosphate rejection were both measured in synthetic single salt and multi-ion mixtures and in anaerobic effluent. The rejection for ammonium (30?95%) is neither sufficient for discharge nor potable water use. The rejection of phosphate (74?99%) is in most cases almost sufficient to meet the standards for potable water. | |
| 09/01/2005 00:00:00 | |
| Link to Article | |
| 4.2.9 | nanofiltration (NF) |
| Phosphorus recovery from sewage sludge with a hybrid process of low pressure wet oxidation and nanofiltration | |
| Abstract Phosphorus recovery from sewage sludge will become increasingly important within the next decades due to depletion of mineral phosphorus resources. In this work a new process concept was investigated, which aims at realising phosphorus recovery in a synergistic way with the overall sewage sludge treatment scheme. This process combines a low pressure wet oxidation for sewage sludge decomposition as well as phosphorus dissolution and a nanofiltration process to separate phosphorus from heavy metals and obtain a clean diluted phosphoric acid, from which phosphorus can be recovered as clean fertiliser. It was shown that this process concept is feasible for sewage sludge for wastewater treatment plants that apply enhanced biological removal or precipitation with alumina salts for phosphorus removal. The critical parameter for phosphorus dissolution in the low pressure wet oxidation process is the iron concentration, while in the nanofiltration multi-valent cations play a predominant role. In total, a phosphorus recovery of 54% was obtained for an exemplary wastewater treatment plant. Costs of the entire process are in the same range as conventional sewage sludge disposal, with the benefit being phosphorus recovery and reduced emission of greenhouse gases due to avoidance of sludge incineration. | |
| 04/01/2012 00:00:00 | |
| Link to Article | |
| 4.2.10 | nanofiltration (NF) |
| Removal of Heavy Metal from Wastewater Using Ion Exchange Membranes | |
| Clean water supplies are vital for industry, agriculture, and energy production. However, the water pollution issue is becoming more serious due to ever-increasing wastewater discharges from the industries into the environment. As the freshwater resource is limited, it is extremely crucial to reuse the wastewater after it has been treated to remove the heavy metal ions and other organic pollutants, which is believed to be the only way to find the new water resource. In view of the significance of treatment of wastewater contaminants, various remediation technologies are proposed and developed for efficient removal of heavy metal ions, including ultrafiltration, nanofiltration, reverse osmosis, forward osmosis, adsorption, electrodialysis method, and fuel cell method. This chapter starts with a brief introduction of heavy metals, which are chromium, nickel, copper, zinc, cadmium, mercury, and lead. Then both physical treatment and chemical treatment are summarized. Finally, the remaining challenges and future perspectives are highlighted. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
| 4.2.11 | nanofiltration (NF) |
| Removal of Heavy Metals from Electroplating Wastewater by Thin-Film Composite Nanofiltration Hollow-Fiber Membranes | |
| In this study, thin-film composite nanofiltration (NF) hollow-fiber membranes were used to remove heavy metals from actual electroplating wastewater. The effects of the operating pressure, feed temperature, and feed pH on the membrane performance for the treatment of electroplating wastewater were investigated. The rejection rates for chromium, copper, and nickel ions reached 95.76%, 95.33%, and 94.99%, respectively, at 0.4 MPa. With a rise in the feed temperature, the permeate flux increased while the rejection rates of heavy metals did not significantly change. It was evident that the feed pH greatly affected the permeate flux and heavy-metal rejection as well. In addition, all of the rejection rates of heavy metals by the membrane were over 94.8% throughout the electroplating wastewater concentration process. Also, the NF hollow-fiber membrane showed good stability in electroplating wastewater with a pH value of 2.31. | |
| 12/11/2013 00:00:00 | |
| Link to Article | |
| 4.2.12 | nanofiltration (NF) |
| Selective separation of chloride and sulfate by nanofiltration for high saline wastewater recycling | |
| Abstract In order to effectively separate chloride (such as NaCl) and sulfate (such as Na 2 SO 4 ) for high saline wastewater recycling, one commercial NF membrane (named Desal-DL) was employed in the permeation of the single and binary salt solutions of NaCl and Na 2 SO 4 with a lab-scale cross-flow batch module, where the salt concentration ranged from 4 to 96 g L −1 and the operating pressures varied from 0.6 to 2.4 MPa as well as the temperature was kept under room temperature. The experimental results showed that the Desal-DL NF membrane had a low rejection to NaCl and a high rejection to Na 2 SO 4 for single salt solutions. While for binary salt solutions, the membrane presented a bit higher rejection to SO 4 2− and much lower rejection to Cl − , even special negative rejection to Cl − was observed when the concentration of Na 2 SO 4 was high. This implies that NF is suitable to be used for the separation of Na 2 SO 4 and NaCl from their binary solution, where Na 2 SO 4 could be retained by the NF membrane and concentrated to high concentration while NaCl could pass through the membrane and might be diluted to low concentration with a diafiltration operation mode. Finally the selective separation of Na 2 SO 4 and NaCl by NF diafiltration was simulated for the binary salt solution containing 23.4 g L −1 NaCl and 8.76 g L −1 Na 2 SO 4 . A highly concentrated solution of Na 2 SO 4 (71.74 g L −1 ) and a relatively pure solution of NaCl (20.79 g L −1 ) were obtained, which favored the post-treatment of high saline wastewater for inorganic salts recycling. | |
| 06/01/2016 00:00:00 | |
| Link to Article | |
| 4.2.13 | nanofiltration (NF) |
| The formation and characterisation of an asymmetric nanofiltration membrane for ammonia-nitrogen removal: effect of shear rate. | |
| Abstract The focus of this research is to study the potential of nanofiltration membrane technology in removing ammonia–nitrogen from the aquaculture system. One of the major fabrication parameters that directly affect the separation performance is shear rate or casting rate during membrane fabrication. In this study, asymmetric polyethersulfone (PES) nanofiltration membranes were prepared at five different shear rates within the range of 67–400 s −1 . Membrane productivity and separation performance were assessed via pure water, salt and ammonia–nitrogen permeation experiments, and their structural properties were determined by employing the combination of the irreversible thermodynamic (IT) model, solution diffusion model, steric hindrance pore (SHP) model and Teorell–Meyers (TMS) model. The study reveals that the alteration of shear rate enormously affects the membrane morphology and structural parameters, hence subsequently significantly influencing the membrane performance. It was found that, membrane produced at the shear rate 200 s −1 or equivalent to 10 s of casting speed during membrane fabrications managed to remove about 68% of ammonia–nitrogen, in which its separation performance is the most favourable by means of highest flux and rejection ability towards unwanted solutes. Besides, from the research findings, nano-membrane technology is a potential candidate for the treatment of aquaculture wastewater. | |
| 03/01/2010 00:00:00 | |
| Link to Article | |
| 4.2.14 | nanofiltration (NF) |
| Thin-Film Nanocomposite Nanofiltration Membranes Incorporated with Graphene Oxide for Phosphorus Removal | |
| For the first time, thin film nanocomposite (TFN) nanofiltration membranes incorporated with graphene oxide (GO) were synthesized and used to separate phosphorus from water source of different properties. Prior to phosphorus removal tests, the properties of the two TFN membranes (TFN-1 and TFN-2 with GO loadings of 0.15 and 0.3 wt%, respectively) and one control thin film composite (TFC) membrane were subject to standard characterizations to determine pure water flux, salt rejection, surface hydrophilicity, pore size and porosity. Results showed that upon incorporation of GO, the water flux of composite membrane could be significantly improved with minimum decrease in salt rejection. This is mainly due to improved surface hydrophilicity coupled with enlarged pore size and overall structural porosity. The TFN-1 membrane in particular is found to perform better owing to its good combination of water flux and solute rejection. When tested with feed solution containing 10 mg L-1 phosphorus, the TFN-1 membrane showed water flux of 13.2 L m-2 h-1, i.e., 17.9% higher than the water flux achieved by the TFC membrane. Its total phosphorus rejection meanwhile recorded at 80% compared to 84% achieved by the TFC membrane. The TFN-1 membrane also exhibited higher water flux and comparable phosphorus rejection in comparison to the TFC membrane when both membranes were used to treat phosphorus solution containing humic acids. Although the incorporation of GO tended to produce the TFN membrane with larger surface pore size, the significant improvement in membrane water flux and surface hydrophilicity had outweighed the small decrease in phosphorus removal rate. | |
| 02/01/2018 00:00:00 | |
| Link to Article | |
4.3 Reverse osmosis
Formally, reverse osmosis is the process of forcing a solvent from a region of high solute concentration through a semipermeable membrane to a region of low-solute concentration by applying a pressure in excess of the osmotic pressure.[\[Wiki\]](https://en.wikipedia.org/wiki/Reverse_osmosis#:\~:text=Formally%2C%20reverse%20osmosis%20is%20the,excess%20of%20the%20osmotic%20pressure.)
Reverse Osmosis can be performant at removing low level of heavy metals, although in aerobic conditions metal oxides can clog the membranes. Also, RO is not a very cost efficient method, unless the water salt content requires further demineralisation.[\[Source\]](https://www.lenntech.com/processes/heavy/heavy_metals_removal.htm#ixzz6RaPbx6Nm)
"One of the hottest new technologies on the bench in laboratories in the U.K., Saudi Arabia, and South Korea and elsewhere is one-atom thick, perforated graphene membranes that can cut reverse osmosis desalination to a fraction of its current cost. Developed at the Massachusetts Institute of Technology, the membrane’s pores can be tuned to optimize permeability. The hang-up for now is how to mass-produce the material," [\[Source\]](https://www.wateronline.com/doc/reverse-osmosis-expensive-inefficient-obsolete-0001)
**Highlights:**
* RO is pressure driven technique used to remove dissolved solids and smaller particles; RO is only permeable to water molecules. The applied pressure on RO must be enough so that water can be able to overcome the osmotic pressure. The pore structure of RO membranes is much tighter than UF, they convert hard water to soft water, and they are practically capable of removing all particles, bacteria and organics, it requires less maintenance. Some disadvantages include the use of high pressure, RO membranes are expensive compared to other membrane processes and are also prone to fouling. In some cases, high level of pre-treatment is required. RO has extremely small pores and able to remove particles smaller than 0.1 nm. Huang and others, reported **RO membranes coated with azide functionalized graphene oxide hence created smooth, antibacterial and hydrophilic membrane, which removed Escherichia coli and reduced BSA fouling.** [\[Paper\]](https://www.intechopen.com/books/wastewater-and-water-quality/wastewater-treatment-using-membrane-technology)
**Heavy metals:**
* In this study, **low-pressure reverse osmosis was analyzed to remove heavy metal ions (nickel and copper) from highly diluted feed flows.** Given the ability of these ions to form complexes with EDTA, the effectiveness of a preliminary stage of complexation was also evaluated. The experimental system consisted of a reactor with commercial flat membrane of polyamide and cross flow. Studies employing solutions of single ions and also mixture of ions in different concentration ranges reached removals of 99%. [ \[Art. #ARTNUM\]](#article-96290-2311502662)
* The results showed that high removal efficiency of the heavy metals could be achieved by RO process (98% and 99% for copper and cadmium, respectively). [\[Paper\]](https://www.sciencedirect.com/science/article/pii/S1878535210001334#s0055)
* R.O is a membrane filtration process where water can easily pass through a membrane however cationic compounds are retained. The pore size of the R.O membrane is 0.1nm. R.O can be used for all solutions which have less quantity of metal dissolved in the millimolar or micromolar range. [\[Paper\]](https://www.researchgate.net/publication/331952883_Remediation_of_Nickel_ion_from_wastewater_by_applying_various_techniques_a_review)
* In this study, **the operating conditions and synergistic effect of salts and natural organic matter (NOM) on removal of metal cations (Cd, Cu, Ni, and Pb) in reverse osmosis (RO) concentrate** and synthetic solutions were investigated using DWTS (drinking water treatment solids). The amount of heavy metals removed from concentrate increased with increasing pH and initial metal concentration. Cu and Pb were almost completely removed by sorption and precipitation. **Higher concentrations of NaCl, CaCl 2 , Na 2 SO 4 , and presence of NOM in RO concentrate decreased the sorption of Cd and Ni due to ion competition, complex formation, and simultaneous chelation.** This study demonstrated using DWTS to adsorb heavy metals from desalination concentrate is an environmental friendly and economical approach for sustainable management of concentrate. [\[Art. #ARTNUM\]](#article-96290-2590513763)
* In this study, the ability of carbon nanotube membranes in separating three heavy metal ions from aqueous solutions, namely Zn2+, Ni2+, and Cd2+, under reverse osmosis process is investigated by using molecular dynamics simulation. Also, the impact of the type of heavy metal ion on the number of water molecules moving through membranes is evaluated. The simulation results ascertained that the highest number of water molecules is separated in the presence of nickel ion. Finally, the carbon nanotube membrane with chirality of (8, 8) under 200 MPa is introduced as the most appropriate choice for eliminating the heavy ions from water. [\[Art. #ARTNUM\]](#article-96290-2940696262)
* In this study by researchers in Singapore and Saudi Arabia, a novel forward osmosis (FO) process for the removal of heavy metal ions from wastewater has been demonstrated for the first time. The proposed FO process consists of a thin-film composite (TFC) FO membrane made from interfacial polymerisation on a macrovoid-free polyimide support, and a novel bulky hydroacid complex Na~4~\[Co(C~6~H~4~O~7~)~2~\]·2H~2~O (referred to as Na–Co–CA) as the draw solute to minimise reverse solute flux. [\[Paper\]](https://www.filtsep.com/water-and-wastewater/features/novel-forward-osmosis-process-for-effective/)
**Nutrients:**
* Swine wastewater: Two types of spiral-wound RO membranes were tested and compared. The RO was found to be highly effective in separating nutrient and salt elements from water. **After RO treatment, over 70% of NH3 -N, NO2 -N, and NO3 -N and over 90% of other elements, such as P, K, Cl, Ca, Mg, Na, Zn, Fe, and Cu, were concentrated in a liquid effluent with one-tenth the original volume.** [\[Art. #ARTNUM\]](#article-96290-2060507039)
* Nanofiltration (NF) and reverse osmosis (RO) membranes might be used to recover the nutrients from anaerobically treated black water. The permeate might be used in a water reuse scheme. The focus of this paper is to test commercially available NF and RO membranes to remove nutrients from anaerobically treated black water in order to meet the Dutch guidelines. A large number of commercial tubular, capillary and flat sheet NF and RO membranes was tested on laboratory scale on their performance to meet the Dutch guidelines for ammonium and phosphate. The ammonium and phosphate concentrations used were based on the effluent composition of anaerobically treated black water. Ammonium and phosphate rejection were both measured in synthetic single salt and multi-ion mixtures and in anaerobic effluent. The rejection for ammonium (30-95%) is neither sufficient for discharge nor potable water use. The rejection of phosphate (74-99%) is in most cases almost sufficient to meet the standards for potable water. [\[Art. #ARTNUM\]](#article-96290-2000756297)
* Liquid wastes from landfills, termed landfill leachates, must be managed on a daily basis and for many years after a landfill is closed. Reverse osmosis (RO) is an experimental method for landfill leachate treatment. At the Alachua County Southwest Landfill, the process uses a two-stage RO filtration system to reduce ammoniacal nitrogen to groundwater cleanup target levels. Pairing RO with algal bioremediation may eliminate the need for the second RO treatment step. [\[Art. #ARTNUM\]](#article-96290-2734467687)
Suppliers
| 4.3.1 | Reverse osmosis |
|---|---|
| Application of reverse osmosis process associated with EDTA complexation for nickel and copper removal from wastewater | |
| AbstractIn this study, low-pressure reverse osmosis was analyzed to remove heavy metal ions (nickel and copper) from highly diluted feed flows. Given the ability of these ions to form complexes with EDTA, the effectiveness of a preliminary stage of complexation was also evaluated. The experimental system consisted of a reactor with commercial flat membrane of polyamide and cross flow. Studies employing solutions of single ions and also mixture of ions in different concentration ranges reached removals of 99%. The complexing agent forms a larger complex than the single ion in aqueous phase, thus increasing ion removal in terms of final concentration in permeate. Experiments made at different pressures showed the increase in pressure has an effect on increasing rejection and permeate flow, but the applied pressure of 0.5 MPa is sufficient to achieve 98.5% removal of metal ions and a flow of about 13 L/h m2. | |
| 09/01/2016 00:00:00 | |
| Link to Article | |
| 4.3.2 | Reverse osmosis |
| Essential Nutrient Additions for Algal Bioremediation of Reverse Osmosis Treated Landfill Leachate | |
| Liquid wastes from landfills, termed landfill leachates, must be managed on a daily basis and for many years after a landfill is closed. Reverse osmosis (RO) is an experimental method for landfill leachate treatment. At the Alachua County Southwest Landfill, the process uses a two-stage RO filtration system to reduce ammoniacal nitrogen to groundwater cleanup target levels. Pairing RO with algal bioremediation may eliminate the need for the second RO treatment step. Primary RO treatment removes nutrients essential for algal growth and therefore adding nutrients to primary RO permeate should increase both algal growth rates and bioremediation rates. The alga Scenedesmus sp. was cultured in primary RO treated landfill leachate with elemental additions and compared with a control. A customized nutrient medium containing essential macro and micronutrients was shown to provide increased algal growth and remediation rates. Landfill leachate was tested as a source of micronutrients and shown to provide equivalent growth and remediation as the customized micronutrient solution, suggesting that low concentrations of landfill leachate may be a viable option as a micronutrient supplement to support algal bioremediation of RO treated landfill leachate. | |
| 12/12/2014 00:00:00 | |
| Link to Article | |
| 4.3.3 | Reverse osmosis |
| Hybrid membrane systems for secondary effluent polishing for unrestricted reuse for agricultural irrigation | |
| Field experiments are in progress for secondary wastewater upgrading for unrestricted utilization for agricultural irrigation. The integrative approach of secondary effluent polishing is based on using a hybrid UltraFiltration (UF) and Reverse Osmosis (RO) membrane pilot system with a capacity of around 1 m3/hr. The UF effluent is used to feed the RO membranes. The RO permeate is subsequently applied for vegetable irrigation. Field results indicate the importance of the UF component in the removal of the organic matter and the pathogens that are still contained in the secondary effluent. Under specific conditions, when the dissolved solids content is relatively low, regarding sanitary and health aspects, the UF effluent can be applied for unrestricted irrigation. During the RO stage most nutrients are removed, allowing application of the effluent without jeopardizing the soil fertility and the aquifers. Preliminary economic assessment indicates that the extra cost for effluent polishing via the UF stage only is in the range of 5 to 15 US cents/m 3 . The extra cost for the RO stage is also assessed at 10 to 25 US cents/m 3 . The additional cost depends to a large extent on the quality of the incoming raw secondary effluent and local requirements of the command region. | |
| 09/01/2004 00:00:00 | |
| Link to Article | |
| 4.3.4 | Reverse osmosis |
| Innovative use of drinking water treatment solids for heavy metals removal from desalination concentrate: Synergistic effect of salts and natural organic matter | |
| Abstract Concentrate treatment and management is one of the most challenging issues that hinder implementation of water reuse and desalination. Drinking water treatment solids (DWTS) could be an effective low-cost sorbent for removal of heavy metals from desalination concentrate to improve water recovery. It provides an innovative approach to reuse the waste streams generated during drinking water treatment and desalination. In this study, the operating conditions and synergistic effect of salts and natural organic matter (NOM) on removal of metal cations (Cd, Cu, Ni, and Pb) in reverse osmosis (RO) concentrate and synthetic solutions were investigated using DWTS. The amount of heavy metals removed from concentrate increased with increasing pH and initial metal concentration. Cu and Pb were almost completely removed by sorption and precipitation. Higher concentrations of NaCl, CaCl 2 , Na 2 SO 4 , and presence of NOM in RO concentrate decreased the sorption of Cd and Ni due to ion competition, complex formation, and simultaneous chelation. This study demonstrated using DWTS to adsorb heavy metals from desalination concentrate is an environmental friendly and economical approach for sustainable management of concentrate. | |
| 04/01/2017 00:00:00 | |
| Link to Article | |
| 4.3.5 | Reverse osmosis |
| Investigation of the Capability of Carbon Nanotube Membranes in Separating the Heavy Metal Ions from Aqueous Solutions by Molecular Dynamics Simulation | |
| In this study, the ability of carbon nanotube membranes in separating three heavy metal ions from aqueous solutions, namely Zn2+, Ni2+, and Cd2+, under reverse osmosis process is investigated by using molecular dynamics simulation. Also, the impact of the type of heavy metal ion on the number of water molecules moving through membranes is evaluated. The simulation results ascertained that the highest number of water molecules is separated in the presence of nickel ion. Finally, the carbon nanotube membrane with chirality of (8, 8) under 200 MPa is introduced as the most appropriate choice for eliminating the heavy ions from water. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
| 4.3.6 | Reverse osmosis |
| Methods of Removing Heavy Metals from Industrial Wastewater | |
| Methods for treating industrial wastewater containing heavy metals often involve technologies for reduction of toxicity in order to meet technology-based treatment standards. This article was focused on the recently developed and newly applicable various treatment processes for the removal of heavy metals from industrial wastewater. Physico-chemical removal processes such as; adsorption on new adsorbents, ion exchange, membrane filtration, electrodialysis, reverse osmosis, ultrafiltration and photocatalysis were discussed. Their advantages and drawbacks in application were evaluated. In the processes of biological treatments microorganisms play a role of settling solids in the solution. Activated sludge, trickling filters, stabilization ponds are widely used for treating industrial wastewater. Bioadsorption is a new biological method and various low cost bioadsorbents (agricultural waste, forest waste, industrial waste, algae etc.) are used for maximum removal of heavy metals from wastewater. Bioadsorption techniques are eco friendly best solutions for removing heavy metals from wastewater rather than physic-chemical methods. But chemical methods are most suitable treatments for toxic inorganic compounds produced from various industries which cannot removed from any biological and physical techniques. Keywords—heavy metals; removal techniques; | |
| 01/01/2015 00:00:00 | |
| Link to Article | |
| 4.3.7 | Reverse osmosis |
| New trends in removing heavy metals from industrial wastewater | |
| Abstract Innovative processes for treating industrial wastewater containing heavy metals often involve technologies for reduction of toxicity in order to meet technology-based treatment standards. This article reviews the recent developments and technical applicability of various treatments for the removal of heavy metals from industrial wastewater. A particular focus is given to innovative physico-chemical removal processes such as; adsorption on new adsorbents, membrane filtration, electrodialysis, and photocatalysis. Their advantages and limitations in application are evaluated. The main operating conditions such as pH and treatment performance are presented. Published studies of 94 cited references (1999–2008) are reviewed. It is evident from survey that new adsorbents and membrane filtration are the most frequently studied and widely applied for the treatment of metal-contaminated wastewater. However, in the near future, the most promising methods to treat such complex systems will be the photocatalytic ones which consume cheap photons from the UV-near visible region. They induce both degradation of organic pollutants and recovery of metals in one-pot systems. On the other hand, from the conventional processes, lime precipitation has been found as one of the most effective means to treat inorganic effluent with a metal concentration of >1000 mg/L. It is important to note that the overall treatment cost of metal-contaminated water varies, depending on the process employed and the local conditions. In general, the technical applicability, plant simplicity and cost-effectiveness are the key factors in selecting the most suitable treatment for inorganic effluent | |
| 10/01/2011 00:00:00 | |
| Link to Article | |
| 4.3.8 | Reverse osmosis |
| Nutrient removal by NF and RO membranes in a decentralized sanitation system | |
| Decentralized treatment of domestic wastewater offers the possibility of water and nutrient reuse. In a decentralized sanitation system the household wastewater streams are separated in a large diluted stream (gray water) and a small and concentrated stream (black water) containing important nutrients like ammonium and phosphate. Nanofiltration (NF) and reverse osmosis (RO) membranes might be used to recover the nutrients from anaerobically treated black water. The permeate might be used in a water reuse scheme. In case of water reuse the produced permeate should meet guidelines for potable water or meet new guidelines which might be applied in the future for intermediate quality of water, for example toilet flushwater; when this is not possible the permeate should meet guidelines for discharge. The most stringent guidelines apply for ammonium and phosphate. The focus of this paper is to test commercially available NF and RO membranes to remove nutrients from anaerobically treated black water in order to meet the Dutch guidelines. A large number of commercial tubular, capillary and flat sheet NF and RO membranes was tested on laboratory scale on their performance to meet the Dutch guidelines for ammonium and phosphate. The ammonium and phosphate concentrations used were based on the effluent composition of anaerobically treated black water. Ammonium and phosphate rejection were both measured in synthetic single salt and multi-ion mixtures and in anaerobic effluent. The rejection for ammonium (30?95%) is neither sufficient for discharge nor potable water use. The rejection of phosphate (74?99%) is in most cases almost sufficient to meet the standards for potable water. | |
| 09/01/2005 00:00:00 | |
| Link to Article | |
| 4.3.9 | Reverse osmosis |
| Removal of Heavy Metal from Wastewater Using Ion Exchange Membranes | |
| Clean water supplies are vital for industry, agriculture, and energy production. However, the water pollution issue is becoming more serious due to ever-increasing wastewater discharges from the industries into the environment. As the freshwater resource is limited, it is extremely crucial to reuse the wastewater after it has been treated to remove the heavy metal ions and other organic pollutants, which is believed to be the only way to find the new water resource. In view of the significance of treatment of wastewater contaminants, various remediation technologies are proposed and developed for efficient removal of heavy metal ions, including ultrafiltration, nanofiltration, reverse osmosis, forward osmosis, adsorption, electrodialysis method, and fuel cell method. This chapter starts with a brief introduction of heavy metals, which are chromium, nickel, copper, zinc, cadmium, mercury, and lead. Then both physical treatment and chemical treatment are summarized. Finally, the remaining challenges and future perspectives are highlighted. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
| 4.3.10 | Reverse osmosis |
| Treatment of Acid Mine Drainage (AMD) by Ultra-Low-Pressure Reverse Osmosis and Nanofiltration | |
| Secondary treatment of acid mine drainage (AMD) from a copper mine in China which has very low-concentration heavy metal ions and high conductivity (2,800 μs/cm), was attributed to the high concentration of dissolved monovalent and divalent ions. Commercially available polyamide ultra-low pressure reverse osmosis (ULPRO) and nanofiltration (NF) membranes were used to remove heavy metal ions and reclaim AMD. Effects of operation pressure, pH, temperature, water recovery efficiency, and operation time on ULPRO and NF performance were investigated. Experimental results show that the rejection increased with an increase of feed pressure and decreased with an increase of feed temperature, and it is dependent on feed pH. Generally, the rejections of heavy metal and total conductivity were greater than 97 and 96% for the ULPROM tested, respectively, which suggested the suitability of such membrane for AMD for the recovery of heavy metal and reclaiming wastewater. However, NF process was capable of removing about... | |
| 11/01/2007 00:00:00 | |
| Link to Article | |
| 4.3.11 | Reverse osmosis |
| TREATMENT OF SWINE WASTEWATER WITH BIOLOGICAL CONVERSION, FILTRATION, AND REVERSE OSMOSIS: A LABORATORY STUDY | |
| The performance of a bench-scale integrated swine wastewater treatment system was evaluated on the basis of energy recovery, fertilizer production, and water reclamation. The system consisted of one anaerobic sequencing batch reactor (ASBR), one or two aerobic sequencing batch reactors (SBR1 and SBR2), one sludge settling tank, one sand filter, and one reverse osmosis (RO) unit. The system was tested with swine wastewater (approximately 15,000 mg/L volatile solids). The chemical oxygen demand (COD) and solids in the wastewater were reduced by 89% to 97%, and total coliforms and E. coli were reduced by 1 log CFU after treatment with the ASBR and SBRs. The oxidized nitrogen (NO2 -N and NO3 -N) was 14% or 53% of total nitrogen in the wastewater after it passed through SBR1 or SBR1 and SBR2, respectively. The sand filter was used to further reduce the COD and solids, especially suspended solids, prior to RO treatment. Two types of spiral-wound RO membranes were tested and compared. The RO was found to be highly effective in separating nutrient and salt elements from water. After RO treatment, over 70% of NH3 -N, NO2 -N, and NO3 -N and over 90% of other elements, such as P, K, Cl, Ca, Mg, Na, Zn, Fe, and Cu, were concentrated in a liquid effluent with one-tenth the original volume. The reclaimed water needs to be further evaluated for its uses. Various operational cost and maintenance issues associated with individual processes and the overall system need to be addressed when the treatment system is scaled up and evaluated for farm applications. | |
| 01/01/2004 00:00:00 | |
| Link to Article | |
4.4 Electrodialysis
Electrodialysis is used to transport salt ions from one solution through ion-exchange membranes to another solution under the influence of an applied electric potential difference. This is done in a configuration called an electrodialysis cell. [\[Wiki\]](https://en.wikipedia.org/wiki/Electrodialysis)
**Heavy metals:**
* The raffinate generated during copper ore hydrometallurgical processing is difficult to be treated because it is strongly acidic, and has high concentrations of heavy metals (Iron, Zinc, Copper etc). **In this study, a bipolar membrane electrodialysis (BMED) system was studied for treatment of this challenging stream because in which salts can be converted into their corresponding acids and bases, which enables resource recovery in raffinate.** The target was to reuse the raffinate as a leaching influent, to achieve zero discharge of wastewater. It was found that 85.9% of SO42- in the raffinate could be recovered by the formation of H2SO4. **The removal rates of heavy metals were 99.3% (iron), 99.1% (zinc), 99.0% (copper), 84.9% (nickel), 70.6% (chromium), 95.8% (cadmium), and 94.8% (arsenic).** The heavy metal cations were mainly removed in the heavy metals chamber (HMC) and anions were mainly removed in the acid compartment. It was concluded that the raffinate can be used as a leaching solution after treatment and the studied BMED process is an effective technique for the treatment of raffinate.[ \[Art. #ARTNUM\]](#article-96117-2977176722)
* Electro-dialysis is separation method where ions are shifted over ion exchange resin with the help of electricity between two electrodes. Tzanetakis et al. investigate the removal of Cobalt and Nickel from their sulphate solution by using two cation exchange and an anion exchange membrane, a stainless steel cathode and platinum oxide based coated titanium cobalt, a suitable complexing agent is EDTA. [\[Paper\]](https://www.researchgate.net/publication/331952883_Remediation_of_Nickel_ion_from_wastewater_by_applying_various_techniques_a_review)
* Electrodialytic removal of Cd(II) from wastewater sludge, was studied. During the remediation a stirred suspension of wastewater sludge was exposed to an electric dc field. The liquid/solid (mL/g fresh sludge) ratio was between 1.4 and 2. Three experiments were performed where the sludge was suspended in distilled water, citric acidor HNO~3~. The Cd(II) removal in the three experiments was 69%, 70% and 67%, respectively. The experiments were performed for zinc,lead and chromium ions. It was found that performance of an ED cell is almost independent on the type of ions and only depends on the operating conditions and the cell structure. In spite of its limitation, **ED offers advantages for the treatment of wastewater laden with heavy metals such as the ability to produce a highly concentrated stream for recovery and the rejection of undesirable impurities from water.** Moreover, valuable metals such as Cr and Cu can be recovered.[\[Art. #ARTNUM\]](#article-96117-2043219105)
* **The organic matter removal was low compared to the inorganic metal ions for the raw water and the neutralized water.**[\[Paper\]](http://www.i-asem.org/publication_conf/anbre19/ZP.3.NR2571_5988F6.pdf)
* Sewage sludge ash is rich in phosphorus, but the direct use as fertilizer is limited because of inorganic contaminants such as heavy metals and strong bonding of phosphorous in the ash. **Electrodialysis (ED) can be used to recover phosphorus and simultaneously remove heavy metals**. Experiments for stirred ash suspensions utilizing a three compartment cell setup where the anode, cathode and stirred suspension are separated by ion exchange membranes are reported. Simplifying this experimental setup by removing the anion exchange membrane brings the anode in direct contact with the stirred ash suspension. Through this adjustment, half-reactions at the anode contribute to the acidity of the stirred suspension resulting in increased dissolution of both phosphorus and heavy metals (Cd, Cu, Cr, Pb, Zn, Ni) and better separation of most heavy metals from the stirred ash suspension. [\[Art. #ARTNUM\]](#article-96117-1980378680)
**Nutrients:**
* The rinse water of the phosphating process contains high concentrations of salts and low concentrations of organic matter, which means that electrodialysis treatment may be an attractive solution. [\[Art. #ARTNUM\]](#article-96117-2241515304)
* Previous studies proved electrodialysis (ED) to be the **most energetically efficient technology for the removal and concentration of ammonium bicarbonate.** An interesting opportunity to avoid this chemical addition is the employment of a bipolar membrane electrodialysis (BPMED). Through this unique technology, it is possible to simultaneously achieve the concentration of TAN, as well as the regulation of pH without chemicals. [\[Art. #ARTNUM\]](#article-96117-2907165361)
* **Results show that nitrogen removal and recovery by electrodialysis is estimated to lower both initial capital costs and subsequent operation costs than traditional N removal technologies.** [\[Art. #ARTNUM\]](#article-96117-3011553396)
* A novel electrodialysis process (ED) with a magnesium anode was developed, and its feasibility to treat synthetic wastewater with low phosphate concentration was demonstrated in a pilot-scale experimental system. The pilot-scale ED system achieved 95% phosphate removal efficiency in the feed stream, and the phosphate concentration in the product stream was kept at 30 mg L−1 after 280 min with periodically renewing the low-concentrated phosphorus (10 mg L−1) feed stream. The running cost of the ED system was estimated to be $26.51 kg−1 P for synthetic wastewater with 10 mg L−1 P as substrate, mainly resulting from the cost of the loss of the magnesium anode. [\[Art. #ARTNUM\]](#article-96117-3013835773)
* Different from current nutrient recovery technologies of recovering one or two nutrient components (PO 4 3− or NH 4 + ) from wastewater, this study aimed to fractionate various nutrient anions and cations simultaneously, including PO 4 3− , SO 4 2− , NH 4 + , K + , Mg 2+ and Ca 2+ , into several streams. The recovered streams could be further paired together to produce high-value products. A novel electrodialysis process was developed by integrating monovalent selective anion and cation exchange membranes into an electrodialysis stack. Results revealed that nutrient recovery was achieved effectively by fractionating PO 4 3− and SO 4 2− into the anionic product stream, whereas bivalent cations (Mg 2+ and Ca 2+ ) were extracted in the cationic product stream and the monovalent cations (K + and NH 4 + ) were concentrated in the brine stream. [\[Art. #ARTNUM\]](#article-96117-2947013546)
**Membranes:**
* For polymeric membranes, surface modification of the polymer is essential; such surface modification includes grafting, blending and incorporation of nanomaterials such as TiO~2~, ZnO, Al~2~O~3~, carbon nanotubes[ ](https://www.intechopen.com/books/wastewater-and-water-quality/wastewater-treatment-using-membrane-technology#B27)and graphene oxide. **Among these, graphene oxide membranes (GMs) are very promising in water treatment application such as desalination and wastewater treatment, due to their hydrophilic properties, flexibility and high mechanical strength; GMs have been reported to give wide range of pure water flux.** [\[Paper\]](https://www.intechopen.com/books/wastewater-and-water-quality/wastewater-treatment-using-membrane-technology)
* The desalination and treatment of tannery unhairing wastewater by electrodialysis (ED) is investigated **in this research in order to separate, concentrate, recover and reuse low molecular weight charged species (S^2-^, HS^-^, OH^-^, Cl^-^, Ca^2+^, Na^+^ and amino acids), and to separate proteins and recycle treated water. Therefore, a novel electrodialysis membrane configuration was proposed. This was based on a double anti-fouling membrane.** The ED anion exchange membrane (AEM), which is very sensitive to organic fouling, was protected by an ultra filtration membrane impermeable to the negatively charged proteins that could not reach the AEM surface. The experimental results were quite promising, and in spite of only one desalination compartment ED cell; the demineralization efficiency was 56 ± 1.25% (5.5-2.4 mS/cm), with a sensitive removal of sulphide, calcium and chloride. The organic matter (protein, peptides…) was isolated in the dilute compartment. The most important result was the total absence of membrane fouling. The experimental results remarkably proved the initial hypothesis, and suggested promising solutions for industrial pollution, where the membrane processes have never been successful. [\[Paper\]](https://pubmed.ncbi.nlm.nih.gov/29182978/)
* In this study, the preparation of a new, functional anion-exchange membrane (AEM), containing guanidinium groups as the anion-exchanging sites (Gu-100), is described. The functional membrane was also employed in pH-dependent electrodialysis experiments using model dairy wastewater streams. Guanidinium was chosen for its specific binding properties toward oxyanions: e.g., phosphate. Significant differences were observed in the electrodialysis experiments for Gu-0 and Gu-100 at pH 7, showing an enhanced phosphate and citrate transport for Gu-100 in comparison to Gu-0. We conclude that having guanidinium groups as anion-exchange sites improves the selectivity of AEMs. As the presented monomer synthesis strategy is modular, we consider the implementation of functional groups into a polymer-based membrane via the synthesis of tailor-made monomers as an important step toward selective ion transport, which is relevant for various fields, including water treatment processes and fuel cells.[\[Paper\]](https://pure.tudelft.nl/portal/files/49857706/acs.est.8b05558.pdf)
**Electrodyalysis Reversal:**
* Membrane fouling leads to high energy consumption and poor separation efficiency. **The fouling problem has been disqualified also by electrodialysis reversal systems EDR. EDR is similar to ED but the direction of ion flow is reversed periodically to break fouling progress by reversing the polarity of the applied electric current.** This process is not used only for the removal of fouling but also for removing salts in desalination systems. EDR does not require additional chemicals and it increases membrane life. [\[Paper\]](https://www.tojsat.net/journals/tojsat/articles/v06i01/v06i01-14.pdf)
Suppliers
| 4.4.1 | Electrodialysis |
|---|---|
| Comparison of two different electrodialytic cells for separation of phosphorus and heavy metals from sewage sludge ash | |
| Abstract With decreasing availability of phosphorus from primary resources its recovery from waste streams becomes increasingly more important. Sewage sludge ash is rich in phosphorus, but the direct use as fertilizer is limited because of inorganic contaminants such as heavy metals and strong bonding of phosphorous in the ash. Electrodialysis (ED) can be used to recover phosphorus and simultaneously remove heavy metals. The present work is an experimental screening of different options for ED in relation to experimental setup and combination with acid addition. Experiments for stirred ash suspensions utilizing a three compartment cell setup where the anode, cathode and stirred suspension are separated by ion exchange membranes are reported. Simplifying this experimental setup by removing the anion exchange membrane brings the anode in direct contact with the stirred ash suspension. Through this adjustment, half-reactions at the anode contribute to the acidity of the stirred suspension resulting in increased dissolution of both phosphorus and heavy metals (Cd, Cu, Cr, Pb, Zn, Ni) and better separation of most heavy metals from the stirred ash suspension. When the ash is suspended in an acidic solution, these effects increase significantly in early stages of the experiments. The combination of ED in a two compartment setup and initial acidification of the stirred suspension is most effective in dissolving of phosphorus and separation of heavy metals. In this setup, up to 96% of the phosphorus in the ash was dissolved after 7 d. Using the three compartment setup and initially suspending the ash in distilled water, resulted in 53% dissolution of the total recovered phosphorus after 7 d. | |
| 04/01/2015 00:00:00 | |
| Link to Article | |
| 4.4.2 | Electrodialysis |
| Economic analysis of electrodialysis, denitrification, and anammox for nitrogen removal in municipal wastewater treatment | |
| Abstract Technologies to remove nitrogen from wastewater are employed to preserve drinking water and prevent environmental damage. Nitrification/denitrification and partial nitrification-anammox are two accepted nitrogen removal techniques for wastewater treatment plants. These processes require energy for aeration and can release fugitive greenhouse gases in the form of nitrous oxide. Electrodialysis could potentially be used as an alternative to remove ammonium from waste streams, but previous experimentation has concluded that concentrate streams experience rapid scaling and fouling of membranes. This analysis compiles literature values to compare the state-of-the-art of municipal nitrogen removal to the new electrodialysis technique on an economic basis. Results show that nitrogen removal and recovery by electrodialysis is estimated to lower both initial capital costs and subsequent operation costs than traditional N removal technologies. | |
| 07/20/2020 00:00:00 | |
| Link to Article | |
| 4.4.3 | Electrodialysis |
| Electrodialysis Treatment of Phosphate Solutions | |
| An effective way to prevent corrosion of metals and alloys is to coat the substrate material. The phosphating process is usually used to provide a phosphate layer for subsequent application of organic coating systems to metal surfaces, such as steel, zinc, aluminum and others. The phosphating process includes several rinsing processes and ions such as \( {\text{PO}}_{4}^{3-},\;{\text{Fe}}^{2+},\;{\text{Ni}}^{2+}\;{\text{and}}\;{\text{Zn}}^{2+}\) are found in the generated wastewater. Emission reduction and eutrophication control require wastewater treatment to remove phosphorous. There is a range of methods available for reducing phosphate in wastewater. Phosphating effluents are usually treated by physicochemical methods, but biological operations are also frequently used. The concentrations of metallic ions are normally above the environmental limits and the coagulation/precipitation technique is usually applied for their removal. However, the use of membranes in tertiary treatment is a promising technology. The rinse water of the phosphating process contains high concentrations of salts and low concentrations of organic matter, which means that electrodialysis treatment may be an attractive solution. | |
| 01/01/2014 00:00:00 | |
| Link to Article | |
| 4.4.4 | Electrodialysis |
| Electrodialysis with bipolar membranes for ammonia recovery in wastewater: An innovative concept for the treatment of ammonia residual streams | |
| Municipal and industrial wastewater contains a significant amount of dissolved nitrogen. This is the results of the organic protein degradation and of the large employment of nitrogen ( N ), usually in the form of ammonia ( NH 3 ), in the industry. Currently, nitrogen is removed in wastewater treatment plant (WWTP) by means of biological treatments. Globally, the most applied treatment consists in the combination of nitrification and denitrification. This technique is characterized by a high energy demand (44.3 MJ per K g NH4 + removed) which accounts for 70% of the total energy consumption in the WWTP. A less energetically intensive alternative treatment is the Anammox process. However, this also presents significant limitations, especially when dealing with extremely polluted stream and in the flexibility of operation. An alternative to reduce the energy cost of nitrogen removal by valorizing the content of residual streams is explored by the N2kWh project. The novel concept underlying the N2kWh project aims to use NH 3 from waste streams as a fuel source for a solid oxide fuel cell (SOFC). In this way, the energy cost for biological N-removal processes is cut, and, ideally, energy can be even produced. WWTP digested reject water was recognized as potential N-source for energy recovery as a result of its relatively high total ammonia nitrogen (TAN) concentrations (up to 1.5 g − N ⋅ L -1 ). A (selective) concentration step and pH regulation are needed in order to convert the TAN in the reject water, mostly present in form of ammonium bicarbonate ( NH 4 HCO 3 ), into NH 3 gas which can be stripped and directly fed in theSOFC. Previous studies proved electrodialysis (ED) to be the most energetically efficient technology for the removal and concentration of ammonium bicarbonate. However, due to the high alkalinity in the obtained concentrate, a large amount of chemicals is required for the pH regulation. An interesting opportunity to avoid this chemical addition is the employment of a bipolar membrane electrodialysis (BPMED). Through this unique technology, it is possible to simultaneously achieve the concentration of TAN, as well as the regulation of pH without chemicals. The main objective of this work was to evaluate the potential of BPMED for the recovery of NH 3 in the boundaries of the N2kWh project. The energy performance of BPMED was compared with the alternative use of conventional ED plus sodium hydroxide for pH control. In order to obtain valuable information on the operation, three setups were employed: regular ED, BPMED and BPMED coupled with two membrane vacuum stripping devices (VMS). For this purpose, a synthetic solution obtained by dissolving 6.6 g ⋅ L -1 NH 4 HCO 3 salt in demiwater was used to simulate the digested reject water. Experiments were designed to characterize the BPMED operation and clarify which processes influence the performance. Experimental laboratory results showed that, in terms of energy consumption for the NH 4 + removal, the BPMED used more energy compared to the ED. The removal of 90% of the initial NH 4 + is achieved by using an average of 13.2±0.1 MJ ⋅ Kg NH4 -1 . This value was 3.3 times higher than that achieved with regular ED. This discrepancy was explained by the extra-elements in the stack and the water dissociation process, responsible for the higher voltage measured during BPMED operation. The energy consumption was proven to be higher also as a consequence of the lower current efficiency for salt transport (73% compared to 95% of conventional ED). This was due to the more severe undesired diffusion processes, mainly gas diffusion and hydroxide leakage from the alkaline stream to the diluate, taking place within the BPMED stack. However, the energy consumption for ammonium removal in BPMED was still more than three times lower than the energy consumed by nitrification-denitrification and comparable to what used by anammox. The implementation of the membrane vacuum stripping modules, in series with the BPMED, only slightly increased the overall current efficiency (up to 3.4 % current efficiency gain). The benefit in current efficiency was less significant for higher concentrations and pH in the alkaline stream. Besides that, the tested technology tandem (BPMED+VMSs) was capable of stripping NH 3 and, consequently, reduce the gas diffusion over the stack. The energy consumed for the production of NH 3 and for the ED operation to reach a pre-defined pH and TAN concentration was estimated to be equal to 82.55 W ℎ per L of concentrate. This value was substantially higher than what consumed by BPMED (48.7 W ℎ) to achieve the same result in the alkaline stream. To conclude, the studied BPMED system was demonstrated to be superior in terms of energy consumption for the recovery of NH 3 gas when compared to the combination of ED and chemical addition. BPMED showed also crucial advantages for the environment, design and safety of the treatment facility. The energy consumption for the removal of nitrogen with BPMED was proven to be lower than what used in the competitive biological technology. Finally, neither the technology nor the operation methods employed were specifically designed/optimized for this application. This made the use of BPMED for the N2kWh purpose even more interesting and promising. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
| 4.4.5 | Electrodialysis |
| Fractionating various nutrient ions for resource recovery from swine wastewater using simultaneous anionic and cationic selective-electrodialysis | |
| Abstract Different from current nutrient recovery technologies of recovering one or two nutrient components (PO 4 3− or NH 4 + ) from wastewater, this study aimed to fractionate various nutrient anions and cations simultaneously, including PO 4 3− , SO 4 2− , NH 4 + , K + , Mg 2+ and Ca 2+ , into several streams. The recovered streams could be further paired together to produce high-value products. A novel electrodialysis process was developed by integrating monovalent selective anion and cation exchange membranes into an electrodialysis stack. Results revealed that nutrient recovery was achieved effectively by fractionating PO 4 3− and SO 4 2− into the anionic product stream, whereas bivalent cations (Mg 2+ and Ca 2+ ) were extracted in the cationic product stream and the monovalent cations (K + and NH 4 + ) were concentrated in the brine stream. For the permeation capabilities of anions, SO 4 2− and Cl − possessed the higher preference, whereas PO 4 3− permeated the membrane more difficult. As to the cations, the permeation sequence was: NH 4 + ≈K + >Ca 2+ >Mg 2+ ≈Na + . Enhancing voltage values not only promoted ion migration rates, but also led to the increase of energy consumption. Although elevating initial phosphate concentration in the anionic product streams from 60 mg/L to 470 mg/L did not influence phosphate fractionation significantly, the current efficiency decreased from 3.55% to 0.65% and a remarkable increased of energy consumption from 29.42 kWh/kg NaH 2 PO 4 to 160.13 kWh/kg NaH 2 PO 4 was observed. Further experiments were conducted for phosphorus recovery by pairing two recovered product streams, which revealed that phosphate precipitation could be achieved by using inherent Ca 2+ and Mg 2+ in the wastewater without dosing external cation sources. | |
| 09/01/2019 00:00:00 | |
| Link to Article | |
| 4.4.6 | Electrodialysis |
| Methods of Removing Heavy Metals from Industrial Wastewater | |
| Methods for treating industrial wastewater containing heavy metals often involve technologies for reduction of toxicity in order to meet technology-based treatment standards. This article was focused on the recently developed and newly applicable various treatment processes for the removal of heavy metals from industrial wastewater. Physico-chemical removal processes such as; adsorption on new adsorbents, ion exchange, membrane filtration, electrodialysis, reverse osmosis, ultrafiltration and photocatalysis were discussed. Their advantages and drawbacks in application were evaluated. In the processes of biological treatments microorganisms play a role of settling solids in the solution. Activated sludge, trickling filters, stabilization ponds are widely used for treating industrial wastewater. Bioadsorption is a new biological method and various low cost bioadsorbents (agricultural waste, forest waste, industrial waste, algae etc.) are used for maximum removal of heavy metals from wastewater. Bioadsorption techniques are eco friendly best solutions for removing heavy metals from wastewater rather than physic-chemical methods. But chemical methods are most suitable treatments for toxic inorganic compounds produced from various industries which cannot removed from any biological and physical techniques. Keywords—heavy metals; removal techniques; | |
| 01/01/2015 00:00:00 | |
| Link to Article | |
| 4.4.7 | Electrodialysis |
| New trends in removing heavy metals from industrial wastewater | |
| Abstract Innovative processes for treating industrial wastewater containing heavy metals often involve technologies for reduction of toxicity in order to meet technology-based treatment standards. This article reviews the recent developments and technical applicability of various treatments for the removal of heavy metals from industrial wastewater. A particular focus is given to innovative physico-chemical removal processes such as; adsorption on new adsorbents, membrane filtration, electrodialysis, and photocatalysis. Their advantages and limitations in application are evaluated. The main operating conditions such as pH and treatment performance are presented. Published studies of 94 cited references (1999–2008) are reviewed. It is evident from survey that new adsorbents and membrane filtration are the most frequently studied and widely applied for the treatment of metal-contaminated wastewater. However, in the near future, the most promising methods to treat such complex systems will be the photocatalytic ones which consume cheap photons from the UV-near visible region. They induce both degradation of organic pollutants and recovery of metals in one-pot systems. On the other hand, from the conventional processes, lime precipitation has been found as one of the most effective means to treat inorganic effluent with a metal concentration of >1000 mg/L. It is important to note that the overall treatment cost of metal-contaminated water varies, depending on the process employed and the local conditions. In general, the technical applicability, plant simplicity and cost-effectiveness are the key factors in selecting the most suitable treatment for inorganic effluent | |
| 10/01/2011 00:00:00 | |
| Link to Article | |
| 4.4.8 | Electrodialysis |
| Phosphorus recovery from sewage sludge ash with bioleaching and electrodialysis | |
| Abstract Phosphorus is an essential element for all living organisms and for plants. However, phosphate rock, which is the main source of phosphorus, is limited and thus it must be recovered from secondary sources like sewage sludge ash (SSA). SSA is one of the most promising secondary sources because it contains considerable amounts of phosphorus. The drawback of SSA as a secondary source is the presence of heavy metals along with phosphorus. In this study, a bioleaching process was applied to solubilize the phosphorus more economically, thus bioleaching bacteria was used to obtain acidic conditions for phosphorus leaching. For this purpose, batch bioleaching experiments were carried out with Sulfur oxidizing bacteria (SOB) to optimize the process in terms of phosphorus dissolution. Experiments were conducted with different amounts of ash, inoculum volumes, and sulfur concentrations. Because the application of the bioleaching process leads to solubilization of heavy metals beside phosphorus, an electrodialysis process was used to separate phosphorus from heavy metals. Electrodialysis experiments were performed in a 3 compartment electrodialysis reactor with gold coated copper electrodes. The maximum phosphorus bioleaching was obtained with 2 g of ash, 40% inoculum, and 10 g.l-1 elemental sulfur. Electrodialysis studies with gold coated copper electrodes lasted for 14 days and 24.6% of the phosphorus was transported to the anode. | |
| 10/01/2019 00:00:00 | |
| Link to Article | |
| 4.4.9 | Electrodialysis |
| Removal of Heavy Metal from Wastewater Using Ion Exchange Membranes | |
| Clean water supplies are vital for industry, agriculture, and energy production. However, the water pollution issue is becoming more serious due to ever-increasing wastewater discharges from the industries into the environment. As the freshwater resource is limited, it is extremely crucial to reuse the wastewater after it has been treated to remove the heavy metal ions and other organic pollutants, which is believed to be the only way to find the new water resource. In view of the significance of treatment of wastewater contaminants, various remediation technologies are proposed and developed for efficient removal of heavy metal ions, including ultrafiltration, nanofiltration, reverse osmosis, forward osmosis, adsorption, electrodialysis method, and fuel cell method. This chapter starts with a brief introduction of heavy metals, which are chromium, nickel, copper, zinc, cadmium, mercury, and lead. Then both physical treatment and chemical treatment are summarized. Finally, the remaining challenges and future perspectives are highlighted. | |
| 01/01/2019 00:00:00 | |
| Link to Article | |
| 4.4.10 | Electrodialysis |
| Separation of Heavy Metals from Leaching Solution of Hospital Waste Incinerator Fly Ash by Electrodialysis | |
| The effects of electric current density, ratio of liquid to solid and treatment time on the removal of heavy metals from the leaching solution of hospital solid waste incineration(HSWI) fly ash by electrodialysis were studied. The characteristics of HSWI fly ash before and after electrodialysis were analyzed. The results show that 11.1% of Pb, 42.3% of Zn, 56.7% of Cd, 38.7% of Cu and 7.5% of Cr were removed from the raw fly ash by optimizing the electrodialytic parameters at the current density 0.8 mA/cm2, ratio of liquid to solid 10 and treatment time 14 d. Under these conditions, the chlorine level decreased from 20.43% in the raw fly ash to 0.78% in the residual ash, loss on ignition of fly ash increased from 11.1% to 34.3% due to the solubilization of soluble compounds like NaCl after electrodialysis. Although some initially existent heavy metals had been removed from the ash during the electrodialysis, the content of heavy metals actually increased due to mineral dissolution and adsorption of activated carbon powder. The exchangeable fraction and carbonate fraction of these heavy metals in the residual ash decreased, but their leaching concentration was above regulatory thresholds of waste landfill. | |
| 01/01/2014 00:00:00 | |
| Link to Article | |
| 4.4.11 | Electrodialysis |
| Study on removal of phosphorus as struvite from synthetic wastewater using a pilot-scale electrodialysis system with magnesium anode | |
| Abstract Struvite precipitation may become ineffective in removing phosphorus due to the low concentration of phosphate in the liquid. In this study, electrolysis with a magnesium anode was applied to recovering phosphorus and ammonia as struvite from wastewater. A novel electrodialysis process (ED) with a magnesium anode was developed, and its feasibility to treat synthetic wastewater with low phosphate concentration was demonstrated in a pilot-scale experimental system. To achieve high phosphate removal efficiency in the product stream, the optimal initial pH and flow rate were found to be 8.8 and 200 L h−1, respectively, for the ED system at a constant current of 0.1 A. The pilot-scale ED system achieved 95% phosphate removal efficiency in the feed stream, and the phosphate concentration in the product stream was kept at 30 mg L−1 after 280 min with periodically renewing the low-concentrated phosphorus (10 mg L−1) feed stream. The running cost of the ED system was estimated to be $26.51 kg−1 P for synthetic wastewater with 10 mg L−1 P as substrate, mainly resulting from the cost of the loss of the magnesium anode. The precipitates generated from the product stream were confirmed as struvite by XRD analysis. | |
| 03/26/2020 00:00:00 | |
| Link to Article | |
| 4.4.12 | Electrodialysis |
| Treatment of raffinate generated via copper ore hydrometallurgical processing using a bipolar membrane electrodialysis system | |
| Abstract The raffinate generated during copper ore hydrometallurgical processing is difficult to be treated because it is strongly acidic, and has high concentrations of heavy metals (Iron, Zinc, Copper etc). In this study, a bipolar membrane electrodialysis (BMED) system was studied for treatment of this challenging stream because in which salts can be converted into their corresponding acids and bases, which enables resource recovery in raffinate. The target was to reuse the raffinate as a leaching influent, to achieve zero discharge of wastewater. It was found that 85.9% of SO42- in the raffinate could be recovered by the formation of H2SO4. The removal rates of heavy metals were 99.3% (iron), 99.1% (zinc), 99.0% (copper), 84.9% (nickel), 70.6% (chromium), 95.8% (cadmium), and 94.8% (arsenic). The heavy metal cations were mainly removed in the heavy metals chamber (HMC) and anions were mainly removed in the acid compartment. A current density of 3.0 mA/cm2, a volume ratio between the raffinate chamber (RC) and the HMC 1:15, and a duration of 40 h were the optimal experimental parameters. Increasing the RC number from one to two and three increased the current efficiency from 54.0% to 106.9% (two) and 157.9% (three), and decreased the specific energy consumption from 0.160 to 0.108 and 0.089 kWh/L of raffinate. It was concluded that the raffinate can be used as a leaching solution after treatment and the studied BMED process is an effective technique for the treatment of raffinate. | |
| 09/01/2019 00:00:00 | |
| Link to Article | |
4.5 Membrane adsorption
A membrane adsorbent is made by connecting functional groups to the surface and pore wall of polymer membranes; the target pollutants are selectively adsorbed to the functional group. The membrane adsorbent effectively combines the filtration performance of the membrane. [\[Paper\]](https://link.springer.com/article/10.1007/s13201-018-0661-6#:\~:text=A%20membrane%20adsorbent%20is%20made,filtration%20performance%20of%20the%20membrane.)
* Application of polymeric membranes for the adsorption of hazardous pollutants may lead to the development of next-generation reusable and portable water purification appliances. **Membranes for membrane adsorption (MA) have the dual function of membrane filtration and adsorption to be very effective to remove trace amounts of pollutants such as cationic heavy metals, anionic phosphates and nitrates.** [\[Art. #ARTNUM\]](#article-96282-2791240048)
**Heavy metals:**
* **The removal of heavy metals using membrane by adsorption is a relatively new method and it has received considerable attention recently.** A number of researches have investigated on adsorptive membrane fabrication and their applications on specific heavy metals adsorption such as Pb, Zn and Cu. This paper reviews the adsorption mechanisms of heavy metals on membranes and several types of adsorbents incorporated in the membranes (carbon source, metal oxides and natural materials) for adsorption enhancement.[\[Review\]](https://aip.scitation.org/doi/abs/10.1063/1.5126540)
* High performance nanofiltration (NF) membranes for heavy metal removal have been molecularly designed by adsorption of chelating polymers containing negatively charged functional groups such as poly (acrylic acid-co-maleic acid) (PAM), poly (acrylic acid) (PAA) and poly (dimethylamine-co-epichlorohydrin-co-ethylenediamine) (PDMED) on the positively charged polyethyleneimine (PEI) cross-linked P84 hollow fiber substrates. **Not only do these chelating polymers change the membrane surface charge and pore size, but also provide an extra mean to remove heavy metal ions through adsorption in addition to traditional steric effect and Donnan exclusion.** The adsorbed membranes have comparable water permeability and superior rejections to heavy metals, for instance, Pb(NO 3 ) 2 , CuSO 4 , NiCl 2 , CdCl 2 , ZnCl 2 , Na 2 Cr 2 O 7 and Na 2 HAsO 4 , with rejections higher than 98%. The membranes also display excellent rejections to mixed ions with rejections more than 99%. The newly developed membranes show reasonably stability during 60-h tests as well as multiple washes. [\[Art. #ARTNUM\]](#article-96282-2066359298)
* In this work, we developed a sulfur-complexed strategy to enhance the removal capability of heavy metal ions using the polyamide nanofiltration membrane by the covalent anchoring of L-cystine and L-cysteine. **The sulfur-functionalized polyamide nanofiltration membrane exhibits superior complexation of heavy metal ions and can efficiently remove them from high-concentration wastewater. As a result, the sulfur-functionalized nanofiltration membrane not only showed excellent desalination performance but also achieved a record removal rate of heavy metal ions (99.99%),** which can effectively reduce Hg(II) concentration from 10 ppm to an extremely low level of 0.18 ppb, well below the acceptable limits in drinking water (2 ppb). [\[Art. #ARTNUM\]](#article-96282-3001732835)
* Heavy metal ions (HMIs) in wastewater can be removed by polyethyleneimine (PEI) adsorption, however, it is difficult to recycle PEI macromolecules from their mixture with suspended particles in wastewater. **A novel HMIs adsorption technique with renewable PEI-grafted porous membranes was developed. PEI molecules were dispersed with high specific area and structured morphology, which allowed HMIs and suspended particles to be retained separately at different locations of the membrane, with the former adsorbed in matrix and the latter rejected on surface.** The membranes with the optimized PEI loading ratio of 30 k wt % behaved excellently with microsphere rejection and Co(II) adsorption reaching 98.5% and 51.0 mg/g, respectively. They successfully decreased Co(II) concentration from 3.0 mg/L to the allowable discharge standard (0.5 mg/L), even with an enhanced flux of 6200 L/m2/h at 0.12 MPa under the cyclic tests. Overall, PEI-grafted membrane adsorption is highly efficient for removing HMIs and suspended particles simultaneously from wastewater.[ \[Art. #ARTNUM\]](#article-96282-2613562196)
* A novel hybrid membrane-adsorption process has been developed for the production of clean water supplies. A 0.2 μm ceramic membrane has been functionalised to produce a super-hydrophilic surface on the microfiltration membrane capable of maintaining flux with little or no fouling under normal operating conditions. **The adsorbent used is a supported epoxidised carbon nanotube material capable of removing heavy metals from solution.** Both the membrane and the adsorbent can be easily cleaned when necessary using only a solution of readily available vinegar.[ \[Art. #ARTNUM\]](#article-96282-2746225960)
* Advanced modified polyacrylonitrile (PAN) membrane with high adsorption property for heavy metal ions was designed and fabricated for the first time. The introduced diazoresin-ethylenediaminetetraacetic acid (DR-EDTA) layer could effectively absorb the metal ion, such as Cu^2+^, Pb^2+^, Hg^2+^ in the waste water. [\[Paper\]](https://www.nature.com/articles/s41598-018-19597-3)
**Phosphate:**
* Membrane adsorption hybrid system (MAHS) was evaluated for the removal of phosphate from a high rate membrane bioreactor (HR-MBR) effluent. The HR-MBR was operated at permeate flux of 30 L/m^2^ h. The results indicated that the HR-MBR could eliminate 93.1 ± 1.5% of DOC while removing less than 53% phosphate (PO~4~-P). Due to low phosphate removal by HR-MBR, a post-treatment of strong base anion exchange resin (Dowex^∗^21K-XLT), and zirconium (IV) hydroxide were used as adsorbent in MAHS for further removal of phosphate from HR-MBR effluent. It was found that the MAHS enabled to eliminate more than 85% of PO~4~-P from HR-MBR effluent. [\[Paper\]](https://www.sciencedirect.com/science/article/pii/S0960852415015783)
Suppliers
| 4.5.1 | Membrane adsorption |
|---|---|
| A hybrid super hydrophilic ceramic membrane and carbon nanotube adsorption process for clean water production and heavy metal removal and recovery in remote locations | |
| Abstract A novel hybrid membrane-adsorption process has been developed for the production of clean water supplies. A 0.2 μm ceramic membrane has been functionalised to produce a super-hydrophilic surface on the microfiltration membrane capable of maintaining flux with little or no fouling under normal operating conditions. The adsorbent used is a supported epoxidised carbon nanotube material capable of removing heavy metals from solution. Both the membrane and the adsorbent can be easily cleaned when necessary using only a solution of readily available vinegar. The intended aim for this new water production system is for the production of clean water in remote locations, in disaster relief zones and for humanitarian purposes. Laboratory studies have shown that the membrane is capable of maintaining flux over a significant period of time and even when tested with an extreme foulant (used motor oil) performed admirably. The rejection properties of the membrane are as expected for small pore microfiltration, i.e. microbial contamination is easily removed. The adsorbent was shown to remove heavy metals (Cd, Hg, Ni, Co and Pb) to a very high degree (>99.3% in all cases) and was easily regenerated to almost complete adsorptive capacity. The hybrid-process was briefly deployed to the Rio Las Vacas (Guatemala) as part of a basic feasibility study and the unit performed as expected. No microbial contamination was detected in the permeate and the flux was maintained consistently at one third of the clean water flux. This demonstrates the system is capable of microbial removal and has good antifouling properties. | |
| 10/01/2017 00:00:00 | |
| Link to Article | |
| 4.5.2 | Membrane adsorption |
| An L-cystine/L-cysteine impregnated nanofiltration membrane with the superior performance of an anchoring heavy metal in wastewater | |
| Considerable efforts are being made to develop new materials and technologies for the efficient and fast removal of toxic ions in drinking water. In this work, we developed a sulfur-complexed strategy to enhance the removal capability of heavy metal ions using the polyamide nanofiltration membrane by the covalent anchoring of L-cystine and L-cysteine. The sulfur-functionalized polyamide nanofiltration membrane exhibits superior complexation of heavy metal ions and can efficiently remove them from high-concentration wastewater. As a result, the sulfur-functionalized nanofiltration membrane not only showed excellent desalination performance but also achieved a record removal rate of heavy metal ions (99.99%), which can effectively reduce Hg(II) concentration from 10 ppm to an extremely low level of 0.18 ppb, well below the acceptable limits in drinking water (2 ppb). Moreover, the sulfur-functionalized nanofiltration membrane showed an exciting long-term stability and can be easily regenerated without significant loss of Hg(II) removal efficiency even after six cycles. Such outstanding performances were attributed to the synthetic effect of Hg–S coordinative interaction, electrostatic repulsion, and the sieving action of nanopores. These results highlight the tremendous potential of thiol/disulfide-functionalized NF active layer as an appealing platform for removing heavy metal ions from polluted water with high performance in environmental remediation. | |
| 01/01/2020 00:00:00 | |
| Link to Article | |
| 4.5.3 | Membrane adsorption |
| Analysis of PAN and PEGDA Coated Membranes for Filtering Water with Reduced Fouling and Increased Heavy Metal Adsorption | |
| An increase in United States water pollution has been denoted over the past 30 years. With a rise in water pollution, enhanced filtration and heavy metal remediation methods are imperative. Membrane fouling, the process whereby extraneous particles deposit onto a membrane surface and degrade the membrane’s performance, is a major issue facing ultrafiltration. This study’s goals were to enhance membrane flux and anti-fouling performance with a PEGDA filter and to compare the efficiency of PVAm and PEI for heavy metal adsorption. Electrospinning was employed to create membrane platforms for coating and grafting polyethylene glycol diacrylate (PEGDA), N,N’Methylenebisacrylamide (MBAA), cellulose nanofibers (CNF), polyvinyl alcohol (PVAm) and polyethylenimine (PEI). The anti-fouling performance of electrospun PAN membranes was determined by coating the surface with CNF, PEGDA, and MBAA, which were chosen due to their hydrophilic and low-fouling properties. Coating the top layer of the membrane with these hydrophilic polymers achieved a flux that remained constant at the quickest rate, at least 20% quicker than that of polyethersulfone (PES) commercial filters. The membrane containing .02% CNF and 0.2% PEGDA exhibited 90% rejection and 99% recovery, indicating that CNF and PEGDA exhibited better fouling resistance than PES. The high fouling performance of the commercial membranes can be attributed to the highly hydrophobic nature of PES, making it prone to membrane fouling. In order to evaluate heavy metal adsorption membrane performance, electrospun PAN membranes were immersed in concentrations of H 2 SO 4 (50-70 wt%) to introduce negative charges creating bonds between PVAm, PEI, and the PAN membrane. The outcomes of static adsorption tests indicated that PVAm adsorbed heavy metals at a rate that was ~8-30 mg/g greater than PEI. The higher adsorption rate can be attributed to the increased surface area resulting from the grafted PVAm. In the future, a combined PEGDA, PAN, and polyvinyl chloride (PVC) membrane should be designed to adsorb heavy metals while reducing fouling. The efficacy of modified periods of extensive filtration should also be evaluated. | |
| 01/01/2012 00:00:00 | |
| Link to Article | |
| 4.5.4 | Membrane adsorption |
| Chelating polymer modified P84 nanofiltration (NF) hollow fiber membranes for high efficient heavy metal removal | |
| Abstract High performance nanofiltration (NF) membranes for heavy metal removal have been molecularly designed by adsorption of chelating polymers containing negatively charged functional groups such as poly (acrylic acid-co-maleic acid) (PAM), poly (acrylic acid) (PAA) and poly (dimethylamine-co-epichlorohydrin-co-ethylenediamine) (PDMED) on the positively charged polyethyleneimine (PEI) cross-linked P84 hollow fiber substrates. Not only do these chelating polymers change the membrane surface charge and pore size, but also provide an extra mean to remove heavy metal ions through adsorption in addition to traditional steric effect and Donnan exclusion. The adsorbed membranes have comparable water permeability and superior rejections to heavy metals, for instance, Pb(NO 3 ) 2 , CuSO 4 , NiCl 2 , CdCl 2 , ZnCl 2 , Na 2 Cr 2 O 7 and Na 2 HAsO 4 , with rejections higher than 98%. The membranes also display excellent rejections to mixed ions with rejections more than 99%. The newly developed membranes show reasonably stability during 60-h tests as well as multiple washes. | |
| 10/01/2014 00:00:00 | |
| Link to Article | |
| 4.5.5 | Membrane adsorption |
| New trends in removing heavy metals from industrial wastewater | |
| Abstract Innovative processes for treating industrial wastewater containing heavy metals often involve technologies for reduction of toxicity in order to meet technology-based treatment standards. This article reviews the recent developments and technical applicability of various treatments for the removal of heavy metals from industrial wastewater. A particular focus is given to innovative physico-chemical removal processes such as; adsorption on new adsorbents, membrane filtration, electrodialysis, and photocatalysis. Their advantages and limitations in application are evaluated. The main operating conditions such as pH and treatment performance are presented. Published studies of 94 cited references (1999–2008) are reviewed. It is evident from survey that new adsorbents and membrane filtration are the most frequently studied and widely applied for the treatment of metal-contaminated wastewater. However, in the near future, the most promising methods to treat such complex systems will be the photocatalytic ones which consume cheap photons from the UV-near visible region. They induce both degradation of organic pollutants and recovery of metals in one-pot systems. On the other hand, from the conventional processes, lime precipitation has been found as one of the most effective means to treat inorganic effluent with a metal concentration of >1000 mg/L. It is important to note that the overall treatment cost of metal-contaminated water varies, depending on the process employed and the local conditions. In general, the technical applicability, plant simplicity and cost-effectiveness are the key factors in selecting the most suitable treatment for inorganic effluent | |
| 10/01/2011 00:00:00 | |
| Link to Article | |
| 4.5.6 | Membrane adsorption |
| Polyethyleneimine-grafted membranes for simultaneously adsorbing heavy metal ions and rejecting suspended particles in wastewater | |
| Heavy metal ions (HMIs) in wastewater can be removed by polyethyleneimine (PEI) adsorption, however, it is difficult to recycle PEI macromolecules from their mixture with suspended particles in wastewater. A novel HMIs adsorption technique with renewable PEI-grafted porous membranes was developed. PEI molecules were dispersed with high specific area and structured morphology, which allowed HMIs and suspended particles to be retained separately at different locations of the membrane, with the former adsorbed in matrix and the latter rejected on surface. The membranes with the optimized PEI loading ratio of 30 k wt % behaved excellently with microsphere rejection and Co(II) adsorption reaching 98.5% and 51.0 mg/g, respectively. They successfully decreased Co(II) concentration from 3.0 mg/L to the allowable discharge standard (0.5 mg/L), even with an enhanced flux of 6200 L/m2/h at 0.12 MPa under the cyclic tests. Overall, PEI-grafted membrane adsorption is highly efficient for removing HMIs and suspended particles simultaneously from wastewater. © 2017 American Institute of Chemical Engineers AIChE J, 63: 4541–4548, 2017 | |
| 10/01/2017 00:00:00 | |
| Link to Article | |
| 4.5.7 | Membrane adsorption |
| Removal of heavy metals and pollutants by membrane adsorption techniques | |
| Application of polymeric membranes for the adsorption of hazardous pollutants may lead to the development of next-generation reusable and portable water purification appliances. Membranes for membrane adsorption (MA) have the dual function of membrane filtration and adsorption to be very effective to remove trace amounts of pollutants such as cationic heavy metals, anionic phosphates and nitrates. In this review article, recent progresses in the development of MA membranes are surveyed. In addition, recent progresses in the development of advanced adsorbents such as nanoparticles are summarized, since they are potentially useful as fillers in the host membrane to enhance its performance. The future directions of R&D in this field are also shown in the conclusion section. | |
| 03/01/2018 00:00:00 | |
| Link to Article | |
| 4.5.8 | Membrane adsorption |
| Synthesis of carbonaceous nanowire membrane for removing heavy metal ions and high water flux | |
| Abstract This study investigated the hydrothermal synthesis of carbonaceous nanowire membrane (CNM) and its separation performances in terms of adsorbing heavy metals and transmembrane water permeation in water treatment. The hydrothermal dehydration and carbonization of mono-saccharide (glucose; 180 °C, 48 h) can yield one-dimensional (1D) carbonaceous nanowires in the presence of tellurium nanowire template. The subsequent solution-evaporation-self-assembly process results in the formation of macro-scale two-dimensional (2D) hydrophilic CNM sheet with large specific surface area, developed nanoporosity, and abundant superficial oxygen-containing functional groups. Owing to these unique properties, the CNM is shown to be capable of efficiently adsorbing a variety of heavy metals, and highly permeable to water molecules. The CNM synthesized gives precedence over conventional membrane and adsorbents, and demonstrates promise as sustainable nanomaterial for separation of heavy metals from water via membrane adsorption process. | |
| 06/01/2013 00:00:00 | |
| Link to Article | |
| 4.5.9 | Membrane adsorption |
| The adsorptive removal of chromium (VI) in aqueous solution by novel natural zeolite based hollow fibre ceramic membrane | |
| Abstract Adsorption is one of the most efficient ways to remove heavy metal from wastewater. In this study, the adsorptive removal of hexavalent chromium, Cr (VI) from aqueous solution was investigated using natural zeolite, clinoptilolite, in the form of hollow fibre ceramic membrane (HFCM). The HFCM sample was prepared using phase inversion-based extrusion technique and followed by sintering process at different sintering temperatures in the range of 900–1050 °C. The fabricated HFCM was characterised using scanning electron microscopy (SEM), contact angle, water permeability, and mechanical strength for all HFCMs sintered at different temperatures. The adsorption and filtration test of Cr (VI) were performed using an in-house water permeation set up with a dead-end cross-flow permeation test. An asymmetric structure with sponge- and finger-like structures across the cross-section of HFCM was observed using SEM. Based on the characterisation data, 1050 °C was chosen to be the best sintering temperature as the water permeability and mechanical strength of this HFCM were 29.14 L/m 2 ∙h and 50.92 MPa, respectively. The performance of the HFCM in adsorption/filtration was 44% of Cr (VI) removal at the Cr (VI) concentration of 40 mg/L and pH 4. In addition, the mathematical model was also performed in simulating the experimental data obtained from this study. All in all, the natural zeolite-based HFCM has a potential as a single-step Cr (VI) removal by membrane adsorption for the wastewater treatment. | |
| 10/01/2018 00:00:00 | |
| Link to Article | |
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