Removal of cod from oil recovery industry wastewater by the advanced oxidation processes (AOP) based on H2O2

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dc.authorid0000-0002-0156-1657
dc.authorid0000-0002-1457-1504
dc.authorscopusid7004045635
dc.authorscopusid36027469400
dc.authorscopusid14522763100
dc.authorscopusid23979891400
dc.authorwosidDinçer, Ali Rıza/ABA-4507-2020
dc.authorwosidKarakaya, Nusret/ABI-5101-2020
dc.authorwosidGunes, Yalcin/ABA-1290-2020
dc.authorwosidGüneş, Elçin/ABA-1276-2020
dc.authorwosidGüneş, Elçin/ABA-2259-2020
dc.contributor.authorDinçer, Ali Rıza
dc.contributor.authorKarakaya, Nusret
dc.contributor.authorGüneş, Elçin
dc.contributor.authorGüneş, Yalçın
dc.date.accessioned2022-05-11T14:17:09Z
dc.date.available2022-05-11T14:17:09Z
dc.date.issued2008
dc.departmentFakülteler, Çorlu Mühendislik Fakültesi, Çevre Mühendisliği Bölümü
dc.description.abstractThe combinations of H2O2/Fe, UV/H2O2/Fe and UV/H2O2 process were investigated on treatment of oil recovery industry wastewater. Treatment of oil recovery industry wastewater, a typical high pollution strength industrial wastewater (chemical oxygen deman (COD): 21000 mg l(-1), biological oxygen demand (BOD): 8000 mg l(-1), oil and grease:1140 mg l(-1), total dissolved solids (TDS): 37000 mg l(-1), total suspended solids: 2580 mg l(-1)), was carried out by batch oxidation processes. The optimal mass ratio for H2O2/Fe+2 yielding the highest COD removal-was found to be 8.658 corresponding to 200.52 g 1(-1) H2O2 and 23.16 g l(-1) Fe+2 concentrations for 60 minutes reaction time. Fenton process gave a maximum COD reduction of 86% (from 21000 to 2980 mg l(-1)) and the combination of UV/H2O2 gave a COD reduction of 39% (from 21000 to 12730). The percentage of removal, after the total reaction time (3.5h), H2O2: 8.4 g l(-1) and Fe+2 : 0.05g l(-1), in the photo Fenton process, corresponded to 81 % of the total initial COD (4200 mg l(-1)). The oxidative ability of the UV/Fe+2 /H2O2 process (81 %) was greater than that of the UV/H2O2 process (55%) for 80% diluted wastewater. COD removal efficiency for UV/H(2)O2 process (COD/H2O2=1/2 (w/w)) was 90%, 55%, and 39 when initial COD was 1050, 4200, and 21000 mg l(-1), respectively, whereas COD removal was 943, 2320, and 8270 mg l(-1), respectively.
dc.identifier.endpage38
dc.identifier.issn1790-7632
dc.identifier.issue1en_US
dc.identifier.scopus2-s2.0-77953352601
dc.identifier.scopusqualityQ3
dc.identifier.startpage31
dc.identifier.urihttps://hdl.handle.net/20.500.11776/6222
dc.identifier.volume10
dc.identifier.wosWOS:000254825700005
dc.identifier.wosqualityN/A
dc.indekslendigikaynakWeb of Science
dc.indekslendigikaynakScopus
dc.institutionauthorDinçer, Ali Rıza
dc.institutionauthorKarakaya, Nusret
dc.institutionauthorGüneş, Elçin
dc.institutionauthorGüneş, Yalçın
dc.language.isoen
dc.publisherGlobal Network Environmental Science & Technology
dc.relation.ispartofGlobal Nest Journal
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.subjectoil recovery industry
dc.subjectfenton
dc.subjectphoto-fenton
dc.subjectUV plus hydrogen peroxide
dc.subjectFentons Reagent
dc.subjectPhoto
dc.subjectBiodegradability
dc.subjectWastewaters
dc.subjectDegradation
dc.titleRemoval of cod from oil recovery industry wastewater by the advanced oxidation processes (AOP) based on H2O2
dc.typeArticle

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