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COD removal from leachate by electrocoagulation process: treatment with monopolar electrodes in parallel connection
This study examines the removal of chemical oxygen demand (COD) from landfill leachate generated from the municipal landfill site of Bingol, Turkey. The effect of parameters such as current density, pH, and inter-electrode distance during the electrocoagulation (EC) process on COD removal of the pro...
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Published in: | Water science and technology 2018-01, Vol.77 (1), p.177-186 |
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creator | Tanyol, Mehtap Ogedey, Aysenur Oguz, Ensar |
description | This study examines the removal of chemical oxygen demand (COD) from landfill leachate generated from the municipal landfill site of Bingol, Turkey. The effect of parameters such as current density, pH, and inter-electrode distance during the electrocoagulation (EC) process on COD removal of the process was investigated. Moreover, for COD removal, the energy consumption and operating costs were calculated for iron electrode under the EC conditions. COD removal efficiency was 72.13% at the current density of 16 mA m
, pH of 8.05, and the inter-electrode distance of 9 mm at the detention time of 60 min with iron electrode and the COD concentration was reduced from 6,100 mg L
to 1,700 mg L
by EC. The highest value of the electrical energy and electrode consumptions per kg of COD in the optimum conditions were determined as 0.055 kWh kg
COD and 3.43 kg kg
COD and the highest operating cost value was found to be 1.41 US$ kg
COD for 0-60 min time intervals. |
doi_str_mv | 10.2166/wst.2017.528 |
format | article |
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, pH of 8.05, and the inter-electrode distance of 9 mm at the detention time of 60 min with iron electrode and the COD concentration was reduced from 6,100 mg L
to 1,700 mg L
by EC. The highest value of the electrical energy and electrode consumptions per kg of COD in the optimum conditions were determined as 0.055 kWh kg
COD and 3.43 kg kg
COD and the highest operating cost value was found to be 1.41 US$ kg
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, pH of 8.05, and the inter-electrode distance of 9 mm at the detention time of 60 min with iron electrode and the COD concentration was reduced from 6,100 mg L
to 1,700 mg L
by EC. The highest value of the electrical energy and electrode consumptions per kg of COD in the optimum conditions were determined as 0.055 kWh kg
COD and 3.43 kg kg
COD and the highest operating cost value was found to be 1.41 US$ kg
COD for 0-60 min time intervals.</description><subject>Biodegradation</subject><subject>Chemical engineering</subject><subject>Chemical oxygen demand</subject><subject>Costs</subject><subject>Current density</subject><subject>Detention time</subject><subject>Distance</subject><subject>Electrocoagulation</subject><subject>Electrodes</subject><subject>Energy consumption</subject><subject>Energy costs</subject><subject>Fluorides</subject><subject>Hazardous materials</subject><subject>Iron</subject><subject>Landfill</subject><subject>Landfills</subject><subject>Leachates</subject><subject>Methods</subject><subject>Municipal solid waste</subject><subject>Operating costs</subject><subject>Organic chemicals</subject><subject>pH effects</subject><subject>Precipitation</subject><subject>Removal</subject><subject>Sludge</subject><subject>Waste disposal sites</subject><issn>0273-1223</issn><issn>1996-9732</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2018</creationdate><recordtype>article</recordtype><recordid>eNpdkTlPxDAQhS0EYpejo0aWaCjI4iNxYjq0nBISDdSRM5lAVk682A5o_z1GHAXVaDTfPL2ZR8gRZwvBlTr_CHEhGC8Xhai2yJxrrTJdSrFN5kyUMuNCyBnZC2HFGCtlznbJTGgpteJqTsLy8Yp6HNy7sbTzbqAWDbyaiLTZULQI0Ttw5mWyJvZupOvUYggXNHo0ccAx0o8-vtLBjW7trPG_Sy0G2ifeeGMtWgpuHNMgaRyQnc7YgIc_dZ8831w_Le-yh8fb--XlQwayKGOGJVQFYtvqHEWTM1AA0DWKKaG1wS7doMoWCsgrDSBk1xrOC90Z1ckcOJf75PRbN3l-mzDEeugDoLVmRDeFmutKF6XKK5bQk3_oyk1-TO4SpaXSXOUqUWffFHgXgseuXvt-MH5Tc1Z_hVGnMOqvMOoURsKPf0SnZsD2D_79vvwE6giH7g</recordid><startdate>20180101</startdate><enddate>20180101</enddate><creator>Tanyol, Mehtap</creator><creator>Ogedey, Aysenur</creator><creator>Oguz, Ensar</creator><general>IWA Publishing</general><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>3V.</scope><scope>7QH</scope><scope>7UA</scope><scope>7X7</scope><scope>7XB</scope><scope>88E</scope><scope>8FE</scope><scope>8FG</scope><scope>8FI</scope><scope>8FJ</scope><scope>8FK</scope><scope>ABJCF</scope><scope>ABUWG</scope><scope>AFKRA</scope><scope>BENPR</scope><scope>BGLVJ</scope><scope>BHPHI</scope><scope>BKSAR</scope><scope>C1K</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>F1W</scope><scope>FYUFA</scope><scope>GHDGH</scope><scope>H96</scope><scope>H97</scope><scope>HCIFZ</scope><scope>K9.</scope><scope>L.G</scope><scope>L6V</scope><scope>M0S</scope><scope>M1P</scope><scope>M7S</scope><scope>PCBAR</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PTHSS</scope><scope>7X8</scope></search><sort><creationdate>20180101</creationdate><title>COD removal from leachate by electrocoagulation process: treatment with monopolar electrodes in parallel connection</title><author>Tanyol, Mehtap ; 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The effect of parameters such as current density, pH, and inter-electrode distance during the electrocoagulation (EC) process on COD removal of the process was investigated. Moreover, for COD removal, the energy consumption and operating costs were calculated for iron electrode under the EC conditions. COD removal efficiency was 72.13% at the current density of 16 mA m
, pH of 8.05, and the inter-electrode distance of 9 mm at the detention time of 60 min with iron electrode and the COD concentration was reduced from 6,100 mg L
to 1,700 mg L
by EC. The highest value of the electrical energy and electrode consumptions per kg of COD in the optimum conditions were determined as 0.055 kWh kg
COD and 3.43 kg kg
COD and the highest operating cost value was found to be 1.41 US$ kg
COD for 0-60 min time intervals.</abstract><cop>England</cop><pub>IWA Publishing</pub><pmid>29339616</pmid><doi>10.2166/wst.2017.528</doi><tpages>10</tpages><oa>free_for_read</oa></addata></record> |
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source | Alma/SFX Local Collection |
subjects | Biodegradation Chemical engineering Chemical oxygen demand Costs Current density Detention time Distance Electrocoagulation Electrodes Energy consumption Energy costs Fluorides Hazardous materials Iron Landfill Landfills Leachates Methods Municipal solid waste Operating costs Organic chemicals pH effects Precipitation Removal Sludge Waste disposal sites |
title | COD removal from leachate by electrocoagulation process: treatment with monopolar electrodes in parallel connection |
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