Publication: Treatment of jewelry manufacturing effluent containing cyanide using ozone-based photochemical advanced oxidation processes
dc.contributor.author | Kiril Mert, Berna | |
dc.contributor.buuauthor | Sivrioğlu, Özge | |
dc.contributor.buuauthor | Yonar, Taner Yona | |
dc.contributor.buuauthor | Özçiftçi, Saire | |
dc.contributor.department | Uludağ Üniversitesi/Mühendislik Fakültesi/Çevre Mühendisliği Bölümü | |
dc.contributor.orcid | 0000-0002-0387-0656 | |
dc.contributor.orcid | 0000-0001-7974-9986 | |
dc.contributor.researcherid | AAM-8073-2020 | |
dc.contributor.researcherid | AAD-9468-2019 | |
dc.contributor.researcherid | FOT-8901-2022 | |
dc.contributor.scopusid | 56114896700 | |
dc.contributor.scopusid | 6505923781 | |
dc.contributor.scopusid | 56115129400 | |
dc.date.accessioned | 2024-05-24T10:54:31Z | |
dc.date.available | 2024-05-24T10:54:31Z | |
dc.date.issued | 2014-03-04 | |
dc.description.abstract | This article considers Advanced Oxidation Processes involving O-3, O-3/UV, O-3/H2O2/UV, and H2O2/UV to destroy cyanide in jewelry manufacturing wastewaters. All experiments were performed in a semibatch reactor. The results showed that total cyanide can be reduced with different reaction rates, and the decrease of total cyanide can be described by pseudo-first-order kinetics. The reaction was performed under different pH values and H2O2 dosages to find the optimal conditions for the oxidation processes. The ozonation process destroyed total cyanide faster at a pH = 12, whereas ozonation combined with H2O2 and/or UV destroyed cyanide faster at a pH =10. The total cyanide destruction rate in the UV/H2O2 (700 mg/L) treatment was the highest among all studied processes, with removal efficiencies of 99% for CN-, 99% for COD and 99% for TOC. | |
dc.identifier.doi | https://doi.org/10.1080/01919512.2013.860354 | |
dc.identifier.endpage | 205 | |
dc.identifier.issn | 0191-9512 | |
dc.identifier.issn | 1547-6545 | |
dc.identifier.issue | 2 | |
dc.identifier.scopus | 2-s2.0-84898663751 | |
dc.identifier.startpage | 196 | |
dc.identifier.uri | https://www.tandfonline.com/doi/full/10.1080/01919512.2013.860354 | |
dc.identifier.uri | https://hdl.handle.net/11452/41524 | |
dc.identifier.volume | 36 | |
dc.identifier.wos | 000334266500010 | |
dc.indexed.scopus | Scopus | |
dc.indexed.wos | SCIE | |
dc.language.iso | en | |
dc.publisher | Taylor & Francis | |
dc.relation.collaboration | Yurt içi | |
dc.relation.journal | Ozone: Science and Engineering | |
dc.relation.publicationcategory | Makale - Uluslararası Hakemli Dergi | |
dc.rights | info:eu-repo/semantics/closedAccess | |
dc.subject | Advanced oxidation processes | |
dc.subject | Environmental sciences & ecology | |
dc.subject | Cyanide | |
dc.subject | Cyanides | |
dc.subject | Jewelry manufacturing effluent | |
dc.subject | Engineering | |
dc.subject | Ozone | |
dc.subject | Removal efficiencies | |
dc.subject | Uv | |
dc.subject | Pseudo-first order kinetics | |
dc.subject | Batch reactors | |
dc.subject | Ozonation process | |
dc.subject | Effluent treatment | |
dc.subject | Oxidation process | |
dc.subject | Oxidation resistance | |
dc.subject | Optimal conditions | |
dc.subject | Ozone | |
dc.subject | Advanced oxidation processes | |
dc.subject | Ozone water treatment | |
dc.subject | Ozonizatin | |
dc.subject | H2O2 | |
dc.subject | Waste-water | |
dc.subject | Hydrogen-peroxide | |
dc.subject | Aqueous-solution | |
dc.subject | Removal | |
dc.subject | Destruction | |
dc.subject | Degradation | |
dc.subject | Technologies | |
dc.subject | Decomposition | |
dc.subject | Ozonation | |
dc.subject.scopus | Cyanides; Waste Water; Adsorption | |
dc.subject.wos | Engineering, environmental | |
dc.subject.wos | Environmental sciences | |
dc.title | Treatment of jewelry manufacturing effluent containing cyanide using ozone-based photochemical advanced oxidation processes | |
dc.type | Article | |
dspace.entity.type | Publication |
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