Electrochemical oxidation of reverse osmosis concentrate on mixed metal oxide (MMO) titanium coated electrodes

Reverse osmosis (RO) membranes have been successfully applied around the world for wastewater reuse applications. However, RO is a physical separation process, and besides the clean water stream (permeate) a reverse osmosis concentrate (ROC) is produced, usually representing 15–25% of the feed water...

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Veröffentlicht in:Water research (Oxford) 2011-10, Vol.45 (16), p.4951-4959
Hauptverfasser: Bagastyo, Arseto Y., Radjenovic, Jelena, Mu, Yang, Rozendal, René A., Batstone, Damien J., Rabaey, Korneel
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container_issue 16
container_start_page 4951
container_title Water research (Oxford)
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creator Bagastyo, Arseto Y.
Radjenovic, Jelena
Mu, Yang
Rozendal, René A.
Batstone, Damien J.
Rabaey, Korneel
description Reverse osmosis (RO) membranes have been successfully applied around the world for wastewater reuse applications. However, RO is a physical separation process, and besides the clean water stream (permeate) a reverse osmosis concentrate (ROC) is produced, usually representing 15–25% of the feed water flow and containing the organic and inorganic contaminants at higher concentrations. In this study, electrochemical oxidation was investigated for the treatment of ROC generated during the reclamation of municipal wastewater effluent. Using laboratory-scale two-compartment electrochemical systems, five electrode materials (i.e. titanium coated with IrO 2–Ta 2O 5, RuO 2–IrO 2, Pt–IrO 2, PbO 2, and SnO 2–Sb) were tested as anodes in batch mode experiments, using ROC from an advanced water treatment plant. The best oxidation performance was observed for Ti/Pt–IrO 2 anodes, followed by the Ti/SnO 2–Sb and Ti/PbO 2 anodes. The effectiveness of the treatment appears to correlate with the formation of oxidants such as active chlorine (i.e. Cl 2/HClO/ClO −). As a result, electro-generated chlorine led to the abundant formation of harmful by-products such as trihalomethanes (THMs) and haloacetic acids (HAAs), particularly at Ti/SnO 2–Sb and Ti/Pt–IrO 2 anodes. The highest concentration of total HAAs (i.e. 2.7 mg L −1) was measured for the Ti/SnO 2–Sb electrode, after 0.55 Ah L −1 of supplied specific electrical charge. Irrespective of the used material, electrochemical oxidation of ROC needs to be complemented by a polishing treatment to alleviate the release of halogenated by-products. ► Five different anodes were evaluated for the electrochemical oxidation of ROC. ► Ti/Pt–IrO 2 and Ti/SnO 2–Sb outperformed the other electrodes tested in our study. ► The highest formation of THMs and HAAs was observed for Ti/Pt–IrO 2 and Ti/SnO 2–Sb. ► Indirect oxidation by chlorine was a dominant oxidation mechanism for all anodes.
doi_str_mv 10.1016/j.watres.2011.06.039
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However, RO is a physical separation process, and besides the clean water stream (permeate) a reverse osmosis concentrate (ROC) is produced, usually representing 15–25% of the feed water flow and containing the organic and inorganic contaminants at higher concentrations. In this study, electrochemical oxidation was investigated for the treatment of ROC generated during the reclamation of municipal wastewater effluent. Using laboratory-scale two-compartment electrochemical systems, five electrode materials (i.e. titanium coated with IrO 2–Ta 2O 5, RuO 2–IrO 2, Pt–IrO 2, PbO 2, and SnO 2–Sb) were tested as anodes in batch mode experiments, using ROC from an advanced water treatment plant. The best oxidation performance was observed for Ti/Pt–IrO 2 anodes, followed by the Ti/SnO 2–Sb and Ti/PbO 2 anodes. The effectiveness of the treatment appears to correlate with the formation of oxidants such as active chlorine (i.e. Cl 2/HClO/ClO −). As a result, electro-generated chlorine led to the abundant formation of harmful by-products such as trihalomethanes (THMs) and haloacetic acids (HAAs), particularly at Ti/SnO 2–Sb and Ti/Pt–IrO 2 anodes. The highest concentration of total HAAs (i.e. 2.7 mg L −1) was measured for the Ti/SnO 2–Sb electrode, after 0.55 Ah L −1 of supplied specific electrical charge. Irrespective of the used material, electrochemical oxidation of ROC needs to be complemented by a polishing treatment to alleviate the release of halogenated by-products. ► Five different anodes were evaluated for the electrochemical oxidation of ROC. ► Ti/Pt–IrO 2 and Ti/SnO 2–Sb outperformed the other electrodes tested in our study. ► The highest formation of THMs and HAAs was observed for Ti/Pt–IrO 2 and Ti/SnO 2–Sb. ► Indirect oxidation by chlorine was a dominant oxidation mechanism for all anodes.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><pmid>21802107</pmid><doi>10.1016/j.watres.2011.06.039</doi><tpages>9</tpages></addata></record>
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subjects Anode material
Anodes
Applied sciences
Byproducts
Chlorine
Electrochemical oxidation
Electrochemistry
Electrodes
Exact sciences and technology
haloacetic acids
municipal wastewater
Organic pollutants
Osmosis
oxidants
oxidation
Oxidation by-products
Oxidation-Reduction
Oxides - chemistry
Platinum
Pollution
Reverse osmosis
Reverse osmosis concentrates
streams
Titanium
Titanium - chemistry
Waste water
water flow
water reuse
water treatment
Water treatment and pollution
title Electrochemical oxidation of reverse osmosis concentrate on mixed metal oxide (MMO) titanium coated electrodes
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