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Chemical oxygen demand and tannin/lignin removal from paper mill wastewater by electrocoagulation combined with peroxide and hypochlorite treatments

dc.contributor.authorCaglak, Abdulkadir
dc.contributor.authorSari-Erkan, Hanife
dc.contributor.authorEngin, Guleda Onkal
dc.date.accessioned2026-06-27T14:47:44Z
dc.date.issued2024
dc.description.abstractThe present investigation sought to assess the practicality of utilizing a combined pre-treatment approach comprising electrocoagulation, peroxide, and hypochlorite treatments for the removal of chemical oxygen demand (COD) and tannin/lignin from paper mill wastewater. The study aimed to optimize the operating parameters with a view to maximizing the removal efficiencies while minimizing energy consumption. A pair of iron electrodes were used as anode and cathode in the study, and the main operating parameters were determined as initial pH, applied current, treatment time and oxidant dosage/COD ratio. Response surface methodology (RSM) was used to evaluate the effect of these parameters on COD and tannin/lignin removals. The primary findings of the investigation indicated that the integration of electrocoagulation with peroxide and hypochlorite treatments exhibited efficacy in removing COD, tannin/lignin, colour, phenol, and turbidity from paper mill wastewater. The optimized conditions resulted in COD removal efficiencies of 48.13 +/- 2.2% and 29.53 +/- 1.4% for EC with H2O2 and Ca(OCl)(2), respectively. Tannin/lignin removal efficiencies were 92.59 +/- 3.6% and 94.09 +/- 1.8% for EC-H2O2 and EC-Ca(OCl)(2), respectively. The specific energy consumption (SEC) values showed that EC-Ca(OCl)(2) required 7 times more energy than EC-H2O2 for removing 1 kg COD. The principal deduction drawn from the study was that EC-H2O2 pre-treatment demonstrated superior COD removal efficiency and lower energy consumption, while EC-Ca(OCl)(2) pre-treatment exhibited greater efficiency in removing toxic and recalcitrant pollutants. In future studies, it would be useful to conduct research to increase COD removal efficiency in addition to tannin/lignin removal in EC-Ca(OCl)(2) process.en
dc.description.urihttps://doi.org/10.1080/09593330.2023.2206529
dc.identifier.doi10.1080/09593330.2023.2206529
dc.identifier.eissn1479-487X
dc.identifier.endpage3094
dc.identifier.issn0959-3330
dc.identifier.issue15
dc.identifier.pubmed37105959
dc.identifier.startpage3076
dc.identifier.urihttps://hdl.handle.net/20.500.14981/64871
dc.identifier.volume45
dc.identifier.wos000976027300001
dc.language.isoeng
dc.publisherTAYLOR & FRANCIS LTD
dc.relation.ispartofENVIRONMENTAL TECHNOLOGY
dc.subjectPaper mill wastewater
dc.subjecttannin
dc.subjectlignin removal
dc.subjectelectrocoagulation
dc.subjectoxidation
dc.subjectRSM
dc.subjectoptimization
dc.subjectELECTRO-FENTON
dc.subjectSODIUM-HYPOCHLORITE
dc.subjectPHOTO-FENTON
dc.subjectKRAFT PULP
dc.subjectTECHNOLOGY
dc.subjectINDUSTRY
dc.subjectCOLOR
dc.subjectDECOLORIZATION
dc.subjectEnvironmental Sciences & Ecology
dc.titleChemical oxygen demand and tannin/lignin removal from paper mill wastewater by electrocoagulation combined with peroxide and hypochlorite treatments
dc.typeArticle
dspace.entity.typePublication
local.import.sourceWOS

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