Advanced treatment of biologically pretreated coking wastewater by electrochemical oxidation using Ti/RuO2-IrO2 electrodes

Background Electrochemical oxidation has attracted wide attention in wastewater treatment because of its strong oxidation performance and ease of control. This work investigated the feasibility of electrochemical treatment using a Ti/RuO2–IrO2 anode as an advanced treatment of coking wastewater. The...

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Veröffentlicht in:Journal of chemical technology and biotechnology (1986) 2013-08, Vol.88 (8), p.1568-1575
Hauptverfasser: He, Xuwen, Chai, Zhen, Li, Fuping, Zhang, Chunhui, Li, Dong, Li, Jing, Hu, Jianlong
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container_end_page 1575
container_issue 8
container_start_page 1568
container_title Journal of chemical technology and biotechnology (1986)
container_volume 88
creator He, Xuwen
Chai, Zhen
Li, Fuping
Zhang, Chunhui
Li, Dong
Li, Jing
Hu, Jianlong
description Background Electrochemical oxidation has attracted wide attention in wastewater treatment because of its strong oxidation performance and ease of control. This work investigated the feasibility of electrochemical treatment using a Ti/RuO2–IrO2 anode as an advanced treatment of coking wastewater. The influential operating factors including current density (9.6–108.2 mA cm−2) and electrode gap (0.5–2.5 cm) were evaluated. Results The current density and electrodes gap had significant effects on COD and NH4+‐N removal and the energy consumption. The degradation of COD and NH4+‐N followed pseudo‐first‐order kinetics. In most experiments, high levels of NH4+‐N removal (NH4+‐N removal ratio > 95%) was achieved along with moderate mineralization (COD removal ratio: 60–80%). COD (178.0–285.0 mg L‐1) and NH4+‐N (55.0–76.0 mg L‐1) were degraded by 62% and 96%, respectively, at the optimum conditions (electrode gap: 0.5 cm, current density: 15.6 mA cm−2) after 60 min treatment. Under this optimal condition, the corresponding energy consumption was 8.60 kWh m‐3 for effluent meeting the discharge standards. Furthermore, gas chromatography–mass spectrometry (GC‐MS) analysis indicated that this technique could be employed to eliminate bio‐refractory and toxic compounds such as phenanthrene, indole, quinoline and pyrimidine in coking wastewater. Conclusion Ti/RuO2–IrO2 anode systems were confirmed to be effective in advanced treatment of biologically pretreated coking wastewater. © 2012 Society of Chemical Industry
doi_str_mv 10.1002/jctb.4006
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This work investigated the feasibility of electrochemical treatment using a Ti/RuO2–IrO2 anode as an advanced treatment of coking wastewater. The influential operating factors including current density (9.6–108.2 mA cm−2) and electrode gap (0.5–2.5 cm) were evaluated. Results The current density and electrodes gap had significant effects on COD and NH4+‐N removal and the energy consumption. The degradation of COD and NH4+‐N followed pseudo‐first‐order kinetics. In most experiments, high levels of NH4+‐N removal (NH4+‐N removal ratio &gt; 95%) was achieved along with moderate mineralization (COD removal ratio: 60–80%). COD (178.0–285.0 mg L‐1) and NH4+‐N (55.0–76.0 mg L‐1) were degraded by 62% and 96%, respectively, at the optimum conditions (electrode gap: 0.5 cm, current density: 15.6 mA cm−2) after 60 min treatment. Under this optimal condition, the corresponding energy consumption was 8.60 kWh m‐3 for effluent meeting the discharge standards. Furthermore, gas chromatography–mass spectrometry (GC‐MS) analysis indicated that this technique could be employed to eliminate bio‐refractory and toxic compounds such as phenanthrene, indole, quinoline and pyrimidine in coking wastewater. Conclusion Ti/RuO2–IrO2 anode systems were confirmed to be effective in advanced treatment of biologically pretreated coking wastewater. © 2012 Society of Chemical Industry</description><identifier>ISSN: 0268-2575</identifier><identifier>EISSN: 1097-4660</identifier><identifier>DOI: 10.1002/jctb.4006</identifier><identifier>CODEN: JCTBDC</identifier><language>eng</language><publisher>Chichester, UK: John Wiley &amp; Sons, Ltd</publisher><subject>Applied sciences ; Chemical engineering ; COD and NH4+-N ; coking wastewater ; electrochemical oxidation ; energy consumption ; Exact sciences and technology ; General purification processes ; Pollution ; Reactors ; Ti/RuO2-IrO2 electrodes ; Wastewaters ; Water treatment and pollution</subject><ispartof>Journal of chemical technology and biotechnology (1986), 2013-08, Vol.88 (8), p.1568-1575</ispartof><rights>2012 Society of Chemical Industry</rights><rights>2014 INIST-CNRS</rights><rights>2013 Society of Chemical Industry</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Fjctb.4006$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Fjctb.4006$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,780,784,1417,27924,27925,45574,45575</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&amp;idt=27520060$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>He, Xuwen</creatorcontrib><creatorcontrib>Chai, Zhen</creatorcontrib><creatorcontrib>Li, Fuping</creatorcontrib><creatorcontrib>Zhang, Chunhui</creatorcontrib><creatorcontrib>Li, Dong</creatorcontrib><creatorcontrib>Li, Jing</creatorcontrib><creatorcontrib>Hu, Jianlong</creatorcontrib><title>Advanced treatment of biologically pretreated coking wastewater by electrochemical oxidation using Ti/RuO2-IrO2 electrodes</title><title>Journal of chemical technology and biotechnology (1986)</title><addtitle>J. Chem. Technol. Biotechnol</addtitle><description>Background Electrochemical oxidation has attracted wide attention in wastewater treatment because of its strong oxidation performance and ease of control. This work investigated the feasibility of electrochemical treatment using a Ti/RuO2–IrO2 anode as an advanced treatment of coking wastewater. The influential operating factors including current density (9.6–108.2 mA cm−2) and electrode gap (0.5–2.5 cm) were evaluated. Results The current density and electrodes gap had significant effects on COD and NH4+‐N removal and the energy consumption. The degradation of COD and NH4+‐N followed pseudo‐first‐order kinetics. In most experiments, high levels of NH4+‐N removal (NH4+‐N removal ratio &gt; 95%) was achieved along with moderate mineralization (COD removal ratio: 60–80%). COD (178.0–285.0 mg L‐1) and NH4+‐N (55.0–76.0 mg L‐1) were degraded by 62% and 96%, respectively, at the optimum conditions (electrode gap: 0.5 cm, current density: 15.6 mA cm−2) after 60 min treatment. Under this optimal condition, the corresponding energy consumption was 8.60 kWh m‐3 for effluent meeting the discharge standards. Furthermore, gas chromatography–mass spectrometry (GC‐MS) analysis indicated that this technique could be employed to eliminate bio‐refractory and toxic compounds such as phenanthrene, indole, quinoline and pyrimidine in coking wastewater. 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Chem. Technol. Biotechnol</addtitle><date>2013-08</date><risdate>2013</risdate><volume>88</volume><issue>8</issue><spage>1568</spage><epage>1575</epage><pages>1568-1575</pages><issn>0268-2575</issn><eissn>1097-4660</eissn><coden>JCTBDC</coden><abstract>Background Electrochemical oxidation has attracted wide attention in wastewater treatment because of its strong oxidation performance and ease of control. This work investigated the feasibility of electrochemical treatment using a Ti/RuO2–IrO2 anode as an advanced treatment of coking wastewater. The influential operating factors including current density (9.6–108.2 mA cm−2) and electrode gap (0.5–2.5 cm) were evaluated. Results The current density and electrodes gap had significant effects on COD and NH4+‐N removal and the energy consumption. The degradation of COD and NH4+‐N followed pseudo‐first‐order kinetics. In most experiments, high levels of NH4+‐N removal (NH4+‐N removal ratio &gt; 95%) was achieved along with moderate mineralization (COD removal ratio: 60–80%). COD (178.0–285.0 mg L‐1) and NH4+‐N (55.0–76.0 mg L‐1) were degraded by 62% and 96%, respectively, at the optimum conditions (electrode gap: 0.5 cm, current density: 15.6 mA cm−2) after 60 min treatment. Under this optimal condition, the corresponding energy consumption was 8.60 kWh m‐3 for effluent meeting the discharge standards. Furthermore, gas chromatography–mass spectrometry (GC‐MS) analysis indicated that this technique could be employed to eliminate bio‐refractory and toxic compounds such as phenanthrene, indole, quinoline and pyrimidine in coking wastewater. Conclusion Ti/RuO2–IrO2 anode systems were confirmed to be effective in advanced treatment of biologically pretreated coking wastewater. © 2012 Society of Chemical Industry</abstract><cop>Chichester, UK</cop><pub>John Wiley &amp; Sons, Ltd</pub><doi>10.1002/jctb.4006</doi><tpages>8</tpages></addata></record>
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ispartof Journal of chemical technology and biotechnology (1986), 2013-08, Vol.88 (8), p.1568-1575
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1097-4660
language eng
recordid cdi_proquest_journals_1766835652
source Wiley Journals
subjects Applied sciences
Chemical engineering
COD and NH4+-N
coking wastewater
electrochemical oxidation
energy consumption
Exact sciences and technology
General purification processes
Pollution
Reactors
Ti/RuO2-IrO2 electrodes
Wastewaters
Water treatment and pollution
title Advanced treatment of biologically pretreated coking wastewater by electrochemical oxidation using Ti/RuO2-IrO2 electrodes
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