Publication:
Modeling partial oxidation of a commercial textile surfactant formulation with the H2O2/UV-C process

dc.contributor.authorArslan-Alaton, Idil
dc.contributor.authorTugba, Asli Akin
dc.contributor.authorOlmez-Hanci, Tugba
dc.contributor.departmentÇevre Mühendisliği Bölümü
dc.contributor.departmentÇevre Mühendisliği Bölümü
dc.contributor.ituauthorAlaton, İdil Arslan
dc.contributor.ituauthorHancı, Tuğba Ölmez
dc.date.accessioned2026-01-26T01:11:02Z
dc.date.issued2011-03-01
dc.description.abstractIn the present study, the reaction conditions required for the partial oxidation of a commercial nonionic textile surfactant, an alkyl polyethoxylate, with the H(2)O(2)/UV-C treatment process were optimized using central composite design and response surface methodology (CCD-RSM). CCD-RSM allowed for the development of empirical quadratic equations that satisfactorily predicted COD and TOC removal efficiencies under all studied experimental conditions. Analysis of variance revealed that the variables "H(2)O(2) concentration" and "initial surfactant COD" were found to be the process independent parameters most positively and negatively affecting the treatment performance, respectively, whereas the process variable "treatment time" had a smaller influence on COD and TOC removal efficiencies. According to the established polynomial regression models, for the degradation of the nonionic surfactant at an initial COD of 450 mg L(-1) and pH of 10.5, the optimized treatment conditions were 15 mM H(2)O(2) and a reaction time of 80 min. In order to achieve the treatment targets (complete surfactant removal accompanied by 60% COD and TOC elimination to meet the national discharge consents into receiving water bodies) either H(2)O(2) concentration or photochemical treatment time had to be increased. Activated sludge inhibition experiments conducted with nonionic surfactant solution being subjected to photochemical oxidation under optimized reaction conditions indicated that the inhibitory effect of the nonionic surfactant could be completely eliminated during H(2)O(2)/UV-C treatment and the partial degradation intermediates were more biodegradable than the original textile surfactant.
dc.description.urihttps://doi.org/10.1039/c0pp00170h
dc.description.urihttps://pubmed.ncbi.nlm.nih.gov/20877831
dc.description.urihttps://dx.doi.org/10.1039/c0pp00170h
dc.description.urihttps://aperta.ulakbim.gov.tr/record/19031
dc.identifier.doi10.1039/c0pp00170h
dc.identifier.eissn1474-9092
dc.identifier.endpage402
dc.identifier.issn1474-905X
dc.identifier.openairedoi_dedup___::b7a3d7fe4f2065d0ea7cd757a745b051
dc.identifier.orcid0000-0003-4241-5100
dc.identifier.startpage396
dc.identifier.urihttps://hdl.handle.net/11527/55573
dc.identifier.volume10
dc.language.isoeng
dc.publisherSpringer Science and Business Media LLC
dc.relation.ispartofPhotochemical & Photobiological Sciences
dc.rightsOPEN
dc.sdg.typeGoal 6: Clean Water and Sanitation
dc.titleModeling partial oxidation of a commercial textile surfactant formulation with the H2O2/UV-C process
dc.typeArticle
dspace.entity.typePublication
person.identifier.orcid0000-0003-4241-5100
person.identifier.orcid0000-0001-9200-5420

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