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Arsenic Removal From Groundwater Using an Aerated Electrocoagulation Reactor With 3d Al Electrodes in the Presence of Anions

dc.contributor.author Gören, Ayşegül Yağmur
dc.contributor.author Kobya, Mehmet
dc.contributor.other 03.07. Department of Environmental Engineering
dc.contributor.other 03. Faculty of Engineering
dc.contributor.other 01. Izmir Institute of Technology
dc.coverage.doi 10.1016/j.chemosphere.2020.128253
dc.date.accessioned 2021-01-24T18:33:14Z
dc.date.available 2021-01-24T18:33:14Z
dc.date.issued 2021
dc.description.abstract Co-occurrence of arsenic and anions in groundwater causes a severe health problems and combine effects of these pollutants significantly affect performance of treatment process. Thus, this study has been conducted to examine the combine effects of anions on arsenic removal using aerated electrocoagulation (EC) reactor with 3D Al electrodes in groundwater. A 3-level, six factors Box-Behnken experimental design (BBD) was applied to investigate the individual and combine effect of anions and operating time: phosphate (x1: 1–10 mg L?1), silica (x2: 20–80 mg L?1), bicarbonate (x3: 130–670 mg L?1), fluoride (x4: 2–10 mg L?1), boron (x5: 5–10 mg L?1), and operating time (x6: 8–22 min) on desired responses. The specified responses were effluent arsenic concentration (Cf,As), removal efficiency of arsenic (Re), consumptions of energy and electrode (ENC and ELC), operational cost (OC), and adsorption capacity (qe). The optimum operating parameters predicted using BBD were found to be x1: 1.0 mg L?1, x2: 26.0 mg L?1, x3: 651.5 mg L?1, x4: 2.0 mg L?1, x5: 9.9 mg L?1, and x6: 10.5 min considering highest removal efficiency of arsenic and lowest operational cost. Under these operating conditions, the experimental values of Cf,As, Re, ENC, ELC, OC, and qe were found to be 2.82 ?g L?1, 98.6%, 0.411 kWh m?3, 0.0124 kg m?3, 0.098 $ m?3, and 17.65 ?g As (mg Al)?1, respectively. Furthermore, mathematical modelling was conducted using quadratic regression model and response surface analysis was performed to understand the relationship between independent parameters and responses. © 2020 Elsevier Ltd en_US
dc.description.sponsorship The authors would like to express their appreciation for the financial support of TUBITAK (The Scientific and Technical Research Council of Turkey, Project Number = 111Y103). en_US
dc.identifier.doi 10.1016/j.chemosphere.2020.128253 en_US
dc.identifier.issn 0045-6535
dc.identifier.issn 1879-1298
dc.identifier.scopus 2-s2.0-85090415975
dc.identifier.uri https://doi.org/10.1016/j.chemosphere.2020.128253
dc.identifier.uri https://hdl.handle.net/11147/10244
dc.language.iso en en_US
dc.publisher Elsevier en_US
dc.relation.ispartof Chemosphere en_US
dc.rights info:eu-repo/semantics/closedAccess en_US
dc.subject 3D Al ball Electrodes en_US
dc.subject Aerated electrocoagulation en_US
dc.subject Anions en_US
dc.subject Arsenic removal en_US
dc.subject Groundwater en_US
dc.title Arsenic Removal From Groundwater Using an Aerated Electrocoagulation Reactor With 3d Al Electrodes in the Presence of Anions en_US
dc.type Article en_US
dspace.entity.type Publication
gdc.author.institutional Gören, Ayşegül Yağmur
gdc.author.institutional Gören, Ayşegül Yağmur
gdc.coar.access metadata only access
gdc.coar.type text::journal::journal article
gdc.description.department İzmir Institute of Technology. Environmental Engineering en_US
gdc.description.publicationcategory Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı en_US
gdc.description.scopusquality Q1
gdc.description.volume 263 en_US
gdc.description.wosquality Q1
gdc.identifier.openalex W3083200243
gdc.identifier.pmid 33297198
gdc.identifier.wos WOS:000595802200304
gdc.openalex.fwci 7.0
gdc.openalex.normalizedpercentile 0.85
gdc.opencitations.count 54
gdc.scopus.citedcount 54
gdc.wos.citedcount 43
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relation.isAuthorOfPublication.latestForDiscovery 41435986-875e-4288-988e-9bfda779c33a
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