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dc.contributor.authorKobya, M.
dc.contributor.authorOzyonar, F.
dc.contributor.authorDemirbas, E.
dc.contributor.authorSik, E.
dc.contributor.authorOncel, M. S.
dc.date.accessioned2019-07-27T12:10:23Z
dc.date.accessioned2019-07-28T09:56:08Z
dc.date.available2019-07-27T12:10:23Z
dc.date.available2019-07-28T09:56:08Z
dc.date.issued2015
dc.identifier.issn2213-3437
dc.identifier.urihttps://dx.doi.org/10.1016/j.jece.2015.04.014
dc.identifier.urihttps://hdl.handle.net/20.500.12418/7841
dc.descriptionWOS: 000217986800058en_US
dc.description.abstractIn the present study, laboratory scale experiments were conducted with the air-fed electrocoagulation (EC) reactor using iron (Fe) ball and plate anodes in a batch mode to assess their efficiency in the removal of arsenic from Sivas Sarkisla groundwater (SSG). Effects of the operating parameters namely, initial pHi (6.6-8.6), applied current (0.10-0.50 A), area of electrode (210-630 cm(2)), airflow rate (0-6 L/min) and operating time (0-20 min) for Fe ball and plate anodes on the removal efficiency of arsenic were investigated and operating costs for the treated SSG were calculated for each type electrode. The pH did not have significant effect on the arsenic removal in the pH range 6.6-8.6 for both type electrodes, but higher current density, airflow rate and lowest surface area of electrode led removal of arsenic rapidly from SSG. The optimum operating conditions determined to be pH 7.6, 0.30 A, airflow rate of 6 L/min, anode surface area of 210 cm(2) resulted in removal efficiency of 99.3% and operating cost of 1.55 $/m(3) at 20 min (charge density of 360 C/L or 3.731 F/m(3)) for Fe ball electrodes and 96.9% and 0.101 $/m(3) at 6 min (charge density of 108 C/L or 1.119 F/m(3)) for Fe plate electrodes, respectively. As a comparison, Fe plate electrodes performed better for reducing operating time from 20 to 6 min which affected the operating cost considerably. Both type electrodes in the EC were able to bring down arsenic concentration to < 10 mg/L at the optimum operating conditions. (C) 2015 Elsevier Ltd. All rights reserved.en_US
dc.description.sponsorshipTUBITAK-CAYDAG [111Y103]en_US
dc.description.sponsorshipThe authors would like to thank TUBITAK-CAYDAG for financial support of this work under contract 111Y103.en_US
dc.language.isoengen_US
dc.publisherELSEVIER SCI LTDen_US
dc.relation.isversionof10.1016/j.jece.2015.04.014en_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectArsenic removalen_US
dc.subjectElectrocoagulationen_US
dc.subjectIron ball anodesen_US
dc.subjectIron plate anodesen_US
dc.subjectOperating costen_US
dc.titleArsenic removal from groundwater of Sivas-Sarkisla Plain, Turkey by electrocoagulation process: Comparing with iron plate and ball electrodesen_US
dc.typearticleen_US
dc.relation.journalJOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERINGen_US
dc.contributor.department[Kobya, M. -- Oncel, M. S.] Gebze Tech Univ, Dept Environm Engn, TR-41400 Gebze, Turkey -- [Ozyonar, F.] Cumhuriyet Univ, Dept Environm Engn, Sivas, Turkey -- [Demirbas, E. -- Sik, E.] Gebze Tech Univ, Dept Chem, TR-41400 Gebze, Turkeyen_US
dc.contributor.authorIDKOBYA, Mehmet -- 0000-0001-5052-7220en_US
dc.identifier.volume3en_US
dc.identifier.issue2en_US
dc.identifier.endpage1106en_US
dc.identifier.startpage1096en_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US


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