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Electro-activated Persulfate Oxidation of Biodiesel Wastewater Following Acidification Phase: Optimization of Process Parameters Using Box-Behnken Design

dc.contributor.authorYazici Guvenc, Senem
dc.contributor.authorVarank, Gamze
dc.contributor.authorCebi, Aleyna
dc.contributor.authorOzkaya, Bestami
dc.date.accessioned2026-06-27T14:32:50Z
dc.date.issued2021
dc.description.abstractHigh volumes of wastewater with high pollutant concentration form in the transesterification stage of the process applied for biodiesel production from waste vegetable oils. In this study, application of the advanced electrocoagulation process following acidification was investigated in the biodiesel wastewater treatment. Through the acidification step of the sequential process, respectively, 25.4%, 68.7%, and 50.0% removal efficiencies for COD, oil-grease, and volatile fatty acids (VFAs) were obtained. Electro-activated persulfate (EAP) oxidation was modeled and optimized by using the response surface methodology and Box-Behnken design. The effect of independent variables (current, persulfate/COD ratio, time) on COD, oil-grease, VFAs removal, and total cost and the interaction of the variables of the process were determined. The maximum oil-grease removal efficiency predicted by using the model was 98.3% under the optimum conditions (current: 4 A, persulfate/COD: 4.4, and time: 15 min), whereas oil-grease removal efficiency obtained by the verification experiments performed at optimum conditions was found to be 97.2%. Sequential acidification-EAP process is an appropriate treatment method for biodiesel wastewater with high oil-grease concentration, and response surface methodology is a powerful tool for optimizing the operational conditions of EAP oxidation for COD, oil-grease, VFAs removal, and total cost.Graphical abstracten
dc.description.sponsorshipYildiz Technical University-The Scientific Research Projects Coordinatorship [FBA2020-3906]
dc.description.urihttps://doi.org/10.1007/s11270-020-04962-8
dc.identifier.doi10.1007/s11270-020-04962-8
dc.identifier.eissn1573-2932
dc.identifier.issn0049-6979
dc.identifier.issue1
dc.identifier.urihttps://hdl.handle.net/20.500.14981/61906
dc.identifier.volume232
dc.identifier.wos000606494500004
dc.language.isoeng
dc.publisherSPRINGER INT PUBL AG
dc.relation.ispartofWATER AIR AND SOIL POLLUTION
dc.subjectBiodiesel wastewater
dc.subjectAcidification
dc.subjectElectro-activated persulfate
dc.subjectBox-Behnken design
dc.subjectOil-grease
dc.subjectRESPONSE-SURFACE METHODOLOGY
dc.subjectAQUEOUS-SOLUTIONS
dc.subjectFERROUS ION
dc.subjectDEGRADATION
dc.subjectREMOVAL
dc.subjectELECTROCOAGULATION
dc.subjectSULFATE
dc.subjectFENTON
dc.subjectPEROXYMONOSULFATE
dc.subjectDECOLORIZATION
dc.subjectEnvironmental Sciences & Ecology
dc.subjectMeteorology & Atmospheric Sciences
dc.subjectWater Resources
dc.titleElectro-activated Persulfate Oxidation of Biodiesel Wastewater Following Acidification Phase: Optimization of Process Parameters Using Box-Behnken Design
dc.typeArticle
dspace.entity.typePublication
local.import.sourceWOS

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