Treatment of organic peroxide containing wastewater and water recovery by fenton-adsorption and fenton-nanofiltration processes

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dc.authorscopusid7004045635
dc.authorscopusid25924855400
dc.authorscopusid57236578600
dc.authorscopusid57236578700
dc.authorscopusid57237139700
dc.authorwosidCifci, Deniz Izlen/AAH-3383-2020
dc.contributor.authorDinçer, Ali Rıza
dc.contributor.authorÇifçi, Deniz İzlen
dc.contributor.authorCinkaya, Demet Darcan
dc.contributor.authorDülger, Ender
dc.contributor.authorKaraca, Feriha
dc.date.accessioned2022-05-11T14:17:33Z
dc.date.available2022-05-11T14:17:33Z
dc.date.issued2021
dc.departmentFakülteler, Çorlu Mühendislik Fakültesi, Çevre Mühendisliği Bölümü
dc.description.abstractTreatment of organic peroxide-containing chemical industry wastewater by oxidation methods and recovery of water by the adsorption and nanofiltration (NP010) methods were investigated in this study. The COD and TOC removal rates were obtained as 72.8% and 58.0% in Fenton oxidation and were improved to 78.8% and 59.2% using photo-Fenton oxidation in the same conditions after 5 h of oxidation, respectively. The Fenton-treated wastewater was passed through nanofiltration to remove the organics and recover of the wastewater. The maximum COD removal efficiency of the NP010 membrane varied between 25% and 30% at all pH values. At low and high pH values (pH: 2.5 and pH: 11), as the filtration time increased, the COD removal efficiencies increased, and the highest COD removal efficiencies were obtained in the 180th and 210th minutes. The increase in the COD removal over time at low and high pH was related to the thickness of the filter layer and surface load balance accumulated on the filter surface. By Fenton oxidation coupling with adsorption, 81% of COD (decreased from 10,055 mg/L to 1906 mg/L) and 75.2% of TOC (decreased from 2597 mg/L to 645.4 mg/L) removal could be obtained, while 83.3% of COD (decreased from 9978 mg/L to 1664 mg/L) and 71.1% of TOC (decreased from 2597 mg/L to 750 mg/L) removal could be achieved using Fenton oxidation coupling with nanofiltration (P: 4 bar, pH: 11). In nanofiltration, the filtrate amounts were measured as 41.11 L/m(2).h and 38.33 L/m(2).h, respectively, at 4 bar and 6 bar of filter pressure and 30 min of filtration time. The increase in filtration time and filter pressure caused a decrease in the amount of the filtrate due to the rapid clogging of the filter pores.
dc.description.sponsorshipAKPA Kimya
dc.description.sponsorshipThis study was supported by AKPA Kimya (produces organic peroxides, initiators, paint driers). Address:.Istiklal-Kurtpinar OSM Ataturk Street No: 23/159700, Muratli-Tekirdag, Turkey.
dc.identifier.doi10.1016/j.jenvman.2021.113557
dc.identifier.issn0301-4797
dc.identifier.issn1095-8630
dc.identifier.pmid34467860
dc.identifier.scopus2-s2.0-85113732305
dc.identifier.scopusqualityQ1
dc.identifier.urihttps://doi.org/10.1016/j.jenvman.2021.113557
dc.identifier.urihttps://hdl.handle.net/20.500.11776/6396
dc.identifier.volume299
dc.identifier.wosWOS:000704880700002
dc.identifier.wosqualityQ1
dc.indekslendigikaynakWeb of Science
dc.indekslendigikaynakScopus
dc.indekslendigikaynakPubMed
dc.institutionauthorDinçer, Ali Rıza
dc.institutionauthorÇifçi, Deniz İzlen
dc.institutionauthorKaraca, Feriha
dc.language.isoen
dc.publisherAcademic Press Ltd- Elsevier Science Ltd
dc.relation.ispartofJournal of Environmental Management
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.subjectAdsorption
dc.subjectChemical wastewater
dc.subjectFenton
dc.subjectNanofiltration
dc.subjectOrganic peroxide
dc.subjectLandfill Leachate
dc.subjectReverse-Osmosis
dc.subjectHybrid System
dc.subjectRemoval
dc.subjectOxidation
dc.subjectPerformance
dc.subjectEffluent
dc.subjectReuse
dc.subjectCombination
dc.subjectReagent
dc.titleTreatment of organic peroxide containing wastewater and water recovery by fenton-adsorption and fenton-nanofiltration processes
dc.typeArticle

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