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dc.contributor.authorCho, Kangwoo-
dc.contributor.authorChung, Chong Min-
dc.contributor.authorKim, Yun Jung-
dc.contributor.authorHoffmann, Michael R.-
dc.contributor.authorChung, Tai Hak-
dc.date.accessioned2024-01-20T11:30:28Z-
dc.date.available2024-01-20T11:30:28Z-
dc.date.created2021-09-05-
dc.date.issued2013-10-01-
dc.identifier.issn0959-3330-
dc.identifier.urihttps://pubs.kist.re.kr/handle/201004/127552-
dc.description.abstractStringent water treatment criteria and rapidly growing pollutant loads provoke the demand for retrofitting wastewater treatment plants towards a higher capacity. In this study, we assess a two stage alternating aeration (AA) bioreactor equipped with electroflotation (EF) clarifier, for nitrogen removal within a short hydraulic reTENTion time (HRT). The EF under steady solids loading required a minimum unit height and gas:solids ratio of 0.006 for efficient clarification. The separated sludge blanket was further thickened with retaining stability when the cyclic solids loading was smaller than 1.0kgm(-2). In the continuous operation of the bioreactor, the returned activated sludge concentration increased to more than 18,000mgL(-1), while the effluent suspended solids concentration was lowered below 5mgL(-1). Under influent chemical oxygen demand (COD)/total inorganic nitrogen (TIN) concentration of 300/30mgL(-1), the TIN removal efficiency was near 70% with cycle time ratios of 0.17 and 0.27. Under higher influent COD concentration of 500mgL(-1), TIN removal efficiency was found to be 73.4% at a carbon:nitrogen (C:N) ratio of 10 and even higher (80.4%) at a C:N ratio of 16.6. The increased mixed liquor suspended solids concentrations (>6000mgL(-1)) under the high COD loading were efficiently maintained by using the EF clarifier. The results of this study demonstrate that an EF clarifier with a HRT of less than 1 h can support reliable nitrogen removal in the AA process that has a HRT of 6h, even under increasing influent loadings.-
dc.languageEnglish-
dc.publisherTAYLOR & FRANCIS LTD-
dc.subjectDISSOLVED AIR FLOTATION-
dc.subjectACTIVATED-SLUDGE PROCESS-
dc.subjectWASTE-WATER TREATMENT-
dc.subjectINTERMITTENT-AERATION-
dc.subjectELECTROLYTIC BUBBLES-
dc.subjectMEMBRANE BIOREACTOR-
dc.subjectPHOSPHORUS REMOVAL-
dc.subjectDESIGN-
dc.subjectFLOW-
dc.subjectCLARIFICATION-
dc.titleElectroflotation clarifier to enhance nitrogen removal in a two-stage alternating aeration bioreactor-
dc.typeArticle-
dc.identifier.doi10.1080/09593330.2013.788072-
dc.description.journalClass1-
dc.identifier.bibliographicCitationENVIRONMENTAL TECHNOLOGY, v.34, no.19, pp.2769 - 2776-
dc.citation.titleENVIRONMENTAL TECHNOLOGY-
dc.citation.volume34-
dc.citation.number19-
dc.citation.startPage2769-
dc.citation.endPage2776-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.identifier.wosid000329338100011-
dc.identifier.scopusid2-s2.0-84897019850-
dc.relation.journalWebOfScienceCategoryEnvironmental Sciences-
dc.relation.journalResearchAreaEnvironmental Sciences & Ecology-
dc.type.docTypeArticle-
dc.subject.keywordPlusDISSOLVED AIR FLOTATION-
dc.subject.keywordPlusACTIVATED-SLUDGE PROCESS-
dc.subject.keywordPlusWASTE-WATER TREATMENT-
dc.subject.keywordPlusINTERMITTENT-AERATION-
dc.subject.keywordPlusELECTROLYTIC BUBBLES-
dc.subject.keywordPlusMEMBRANE BIOREACTOR-
dc.subject.keywordPlusPHOSPHORUS REMOVAL-
dc.subject.keywordPlusDESIGN-
dc.subject.keywordPlusFLOW-
dc.subject.keywordPlusCLARIFICATION-
dc.subject.keywordAuthorwastewater treatment-
dc.subject.keywordAuthoralternating aeration bioreactor-
dc.subject.keywordAuthorelectroflotation-
dc.subject.keywordAuthoractivated sludge-
dc.subject.keywordAuthornitrogen removal-
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