Hybrid Process Combining Electrocoagulation and Electro-Oxidation Processes for the Treatment of Restaurant Wastewaters
AbstractThe present study investigates the electrocoagulation-electro-oxidation (EC-EO) process for the treatment of restaurant wastewater (RWW) loaded with organic and inorganic matter, oil, grease, and suspensions solids. The EC-EO process was evaluated in terms of its capability to simultaneously...
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Veröffentlicht in: | Journal of environmental engineering (New York, N.Y.) N.Y.), 2012-11, Vol.138 (11), p.1146-1156 |
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description | AbstractThe present study investigates the electrocoagulation-electro-oxidation (EC-EO) process for the treatment of restaurant wastewater (RWW) loaded with organic and inorganic matter, oil, grease, and suspensions solids. The EC-EO process was evaluated in terms of its capability to simultaneously produce an oxidant and coagulant agents by using either iron or aluminum electrodes arranged in a bipolar configuration or graphite electrodes arranged in a monopolar configuration in the same electrolytic cell. Relatively high concentrations of active chlorine (9.6 mg/min) and aluminum (20–40 mg Al/L) or iron (40–60 mg Fe/L) were produced in situ. The best performance for RWW treatment was obtained by using aluminum and graphite plates alternated in the electrode pack and operated at current of 0.4 A during 90 min of treatment with pH adjusted to approximately 7.0. Under these conditions, more than 98% of oil and greases (O&G) were removed, whereas chemical oxygen demand (COD) and biological oxygen demand (BOD) removal reached 90% and 86%, respectively. Likewise, more than 88% of soluble phosphate was removed, and the process was effective in removing turbidity (98%) and suspended solids (98%). The EC-EO process operated under the best conditions involved a total cost of US$1.56±0.01/m3 of treated restaurant effluent. This cost includes energy and electrode consumption, chemicals, and sludge disposal. |
doi_str_mv | 10.1061/(ASCE)EE.1943-7870.0000579 |
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The EC-EO process was evaluated in terms of its capability to simultaneously produce an oxidant and coagulant agents by using either iron or aluminum electrodes arranged in a bipolar configuration or graphite electrodes arranged in a monopolar configuration in the same electrolytic cell. Relatively high concentrations of active chlorine (9.6 mg/min) and aluminum (20–40 mg Al/L) or iron (40–60 mg Fe/L) were produced in situ. The best performance for RWW treatment was obtained by using aluminum and graphite plates alternated in the electrode pack and operated at current of 0.4 A during 90 min of treatment with pH adjusted to approximately 7.0. Under these conditions, more than 98% of oil and greases (O&G) were removed, whereas chemical oxygen demand (COD) and biological oxygen demand (BOD) removal reached 90% and 86%, respectively. Likewise, more than 88% of soluble phosphate was removed, and the process was effective in removing turbidity (98%) and suspended solids (98%). The EC-EO process operated under the best conditions involved a total cost of US$1.56±0.01/m3 of treated restaurant effluent. This cost includes energy and electrode consumption, chemicals, and sludge disposal.</description><identifier>ISSN: 0733-9372</identifier><identifier>EISSN: 1943-7870</identifier><identifier>DOI: 10.1061/(ASCE)EE.1943-7870.0000579</identifier><identifier>CODEN: JOEEDU</identifier><language>eng</language><publisher>Reston, VA: American Society of Civil Engineers</publisher><subject>Aluminum ; Applied sciences ; Electrocoagulation ; Electrodes ; Exact sciences and technology ; General purification processes ; Greases ; Iron ; Oxygen demand ; Pollution ; Restaurants ; Technical Papers ; Wastewater treatment ; Wastewaters ; Water treatment and pollution</subject><ispartof>Journal of environmental engineering (New York, N.Y.), 2012-11, Vol.138 (11), p.1146-1156</ispartof><rights>2012 American Society of Civil Engineers</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a405t-472f5319c3f218bf792ef714ab2b31b6774ce00ec5cd175e756b94e6d5af8c603</citedby><cites>FETCH-LOGICAL-a405t-472f5319c3f218bf792ef714ab2b31b6774ce00ec5cd175e756b94e6d5af8c603</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttp://ascelibrary.org/doi/pdf/10.1061/(ASCE)EE.1943-7870.0000579$$EPDF$$P50$$Gasce$$H</linktopdf><linktohtml>$$Uhttp://ascelibrary.org/doi/abs/10.1061/(ASCE)EE.1943-7870.0000579$$EHTML$$P50$$Gasce$$H</linktohtml><link.rule.ids>314,780,784,27922,27923,75963,75971</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=26606248$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Daghrir, Rimeh</creatorcontrib><creatorcontrib>Drogui, Patrick</creatorcontrib><creatorcontrib>François Blais, Jean</creatorcontrib><creatorcontrib>Mercier, Guy</creatorcontrib><title>Hybrid Process Combining Electrocoagulation and Electro-Oxidation Processes for the Treatment of Restaurant Wastewaters</title><title>Journal of environmental engineering (New York, N.Y.)</title><description>AbstractThe present study investigates the electrocoagulation-electro-oxidation (EC-EO) process for the treatment of restaurant wastewater (RWW) loaded with organic and inorganic matter, oil, grease, and suspensions solids. The EC-EO process was evaluated in terms of its capability to simultaneously produce an oxidant and coagulant agents by using either iron or aluminum electrodes arranged in a bipolar configuration or graphite electrodes arranged in a monopolar configuration in the same electrolytic cell. Relatively high concentrations of active chlorine (9.6 mg/min) and aluminum (20–40 mg Al/L) or iron (40–60 mg Fe/L) were produced in situ. The best performance for RWW treatment was obtained by using aluminum and graphite plates alternated in the electrode pack and operated at current of 0.4 A during 90 min of treatment with pH adjusted to approximately 7.0. Under these conditions, more than 98% of oil and greases (O&G) were removed, whereas chemical oxygen demand (COD) and biological oxygen demand (BOD) removal reached 90% and 86%, respectively. Likewise, more than 88% of soluble phosphate was removed, and the process was effective in removing turbidity (98%) and suspended solids (98%). The EC-EO process operated under the best conditions involved a total cost of US$1.56±0.01/m3 of treated restaurant effluent. This cost includes energy and electrode consumption, chemicals, and sludge disposal.</description><subject>Aluminum</subject><subject>Applied sciences</subject><subject>Electrocoagulation</subject><subject>Electrodes</subject><subject>Exact sciences and technology</subject><subject>General purification processes</subject><subject>Greases</subject><subject>Iron</subject><subject>Oxygen demand</subject><subject>Pollution</subject><subject>Restaurants</subject><subject>Technical Papers</subject><subject>Wastewater treatment</subject><subject>Wastewaters</subject><subject>Water treatment and pollution</subject><issn>0733-9372</issn><issn>1943-7870</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2012</creationdate><recordtype>article</recordtype><recordid>eNqNkU9rGzEQxUVpIa7b7yAKAfewjrT6t9tbMNs4YEhJUnIUWu0o2bBepZIWJ9--MnZ8K3QuYh6_mSfmIfSNkiUlkl4sLu9WzfemWdKas0JViixJLqHqD2h20j6iGVGMFTVT5Rn6HOMzIZTLWs3Qbv3Whr7Dv4K3ECNe-W3bj_34iJsBbMqqN4_TYFLvR2zG7l0ubl777qAeRyFi5wNOT4DvA5i0hTFh7_AtxGSmYHL3YGKCnUkQ4hf0yZkhwtfjO0e_fzb3q3Wxubm6Xl1uCsOJSAVXpROM1pa5klatU3UJTlFu2rJltJVKcQuEgBW2o0qAErKtOchOGFdZSdgcLQ57X4L_M-Wv6G0fLQyDGcFPUdNKcsFKRth_oEKQivFKZvTHAbXBxxjA6ZfQb01405TofTBa74PRTaP3Ieh9CPoYTB4-P_qYaM3g8mlsH08bSimJLHmVOXngMgb62U9hzJc6Ofzb4C9IPaDW</recordid><startdate>20121101</startdate><enddate>20121101</enddate><creator>Daghrir, Rimeh</creator><creator>Drogui, Patrick</creator><creator>François Blais, Jean</creator><creator>Mercier, Guy</creator><general>American Society of Civil Engineers</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>C1K</scope><scope>SOI</scope><scope>7QF</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope><scope>JG9</scope><scope>KR7</scope></search><sort><creationdate>20121101</creationdate><title>Hybrid Process Combining Electrocoagulation and Electro-Oxidation Processes for the Treatment of Restaurant Wastewaters</title><author>Daghrir, Rimeh ; Drogui, Patrick ; François Blais, Jean ; Mercier, Guy</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a405t-472f5319c3f218bf792ef714ab2b31b6774ce00ec5cd175e756b94e6d5af8c603</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2012</creationdate><topic>Aluminum</topic><topic>Applied sciences</topic><topic>Electrocoagulation</topic><topic>Electrodes</topic><topic>Exact sciences and technology</topic><topic>General purification processes</topic><topic>Greases</topic><topic>Iron</topic><topic>Oxygen demand</topic><topic>Pollution</topic><topic>Restaurants</topic><topic>Technical Papers</topic><topic>Wastewater treatment</topic><topic>Wastewaters</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Daghrir, Rimeh</creatorcontrib><creatorcontrib>Drogui, Patrick</creatorcontrib><creatorcontrib>François Blais, Jean</creatorcontrib><creatorcontrib>Mercier, Guy</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><collection>Aluminium Industry Abstracts</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Materials Research Database</collection><collection>Civil Engineering Abstracts</collection><jtitle>Journal of environmental engineering (New York, N.Y.)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Daghrir, Rimeh</au><au>Drogui, Patrick</au><au>François Blais, Jean</au><au>Mercier, Guy</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Hybrid Process Combining Electrocoagulation and Electro-Oxidation Processes for the Treatment of Restaurant Wastewaters</atitle><jtitle>Journal of environmental engineering (New York, N.Y.)</jtitle><date>2012-11-01</date><risdate>2012</risdate><volume>138</volume><issue>11</issue><spage>1146</spage><epage>1156</epage><pages>1146-1156</pages><issn>0733-9372</issn><eissn>1943-7870</eissn><coden>JOEEDU</coden><abstract>AbstractThe present study investigates the electrocoagulation-electro-oxidation (EC-EO) process for the treatment of restaurant wastewater (RWW) loaded with organic and inorganic matter, oil, grease, and suspensions solids. The EC-EO process was evaluated in terms of its capability to simultaneously produce an oxidant and coagulant agents by using either iron or aluminum electrodes arranged in a bipolar configuration or graphite electrodes arranged in a monopolar configuration in the same electrolytic cell. Relatively high concentrations of active chlorine (9.6 mg/min) and aluminum (20–40 mg Al/L) or iron (40–60 mg Fe/L) were produced in situ. The best performance for RWW treatment was obtained by using aluminum and graphite plates alternated in the electrode pack and operated at current of 0.4 A during 90 min of treatment with pH adjusted to approximately 7.0. Under these conditions, more than 98% of oil and greases (O&G) were removed, whereas chemical oxygen demand (COD) and biological oxygen demand (BOD) removal reached 90% and 86%, respectively. Likewise, more than 88% of soluble phosphate was removed, and the process was effective in removing turbidity (98%) and suspended solids (98%). The EC-EO process operated under the best conditions involved a total cost of US$1.56±0.01/m3 of treated restaurant effluent. This cost includes energy and electrode consumption, chemicals, and sludge disposal.</abstract><cop>Reston, VA</cop><pub>American Society of Civil Engineers</pub><doi>10.1061/(ASCE)EE.1943-7870.0000579</doi><tpages>11</tpages></addata></record> |
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source | American Society of Civil Engineers:NESLI2:Journals:2014; Business Source Complete |
subjects | Aluminum Applied sciences Electrocoagulation Electrodes Exact sciences and technology General purification processes Greases Iron Oxygen demand Pollution Restaurants Technical Papers Wastewater treatment Wastewaters Water treatment and pollution |
title | Hybrid Process Combining Electrocoagulation and Electro-Oxidation Processes for the Treatment of Restaurant Wastewaters |
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