A simplified kinetic model for a full scale anaerobic wastewater treatment plant of a sugar factory under unsteady conditions

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dc.authorid0000-0001-9750-1028en_US
dc.contributor.authorAltinay Perendeci N.
dc.contributor.authorTanyolaç A.
dc.contributor.authorSerdar Çelebi S.
dc.date.accessioned2024-07-12T21:46:07Z
dc.date.available2024-07-12T21:46:07Z
dc.date.issued2012en_US
dc.departmentMaltepe Üniversitesien_US
dc.description.abstractA simplified time dependent mathematical model was developed for an industrial a full-scale two stage anaerobic wastewater treatment plant of a sugar factory under unsteady conditions. As an overall approach, a two-step (acidogenesis and methanogenesis) instantaneous mass balance was considered in the model. The reactor equations employed were based on continuous flow well-mixed conditions. Kinetic parameters related to acidogenic and methanogenic reactions were imported from literature studies. The kinetic model was used to simulate MLVSS (mixed liquor volatile suspended solids), VFA (volatile fatty acid) and COD (chemical oxygen demand) equivalent glucose concentrations in hydrolysis tank, and MLVSS, VFA and gas production in anaerobic tank by making use of data from the full-scale anaerobic methane production plant. The model satisfactorily predicted the measured variables in the hydrolysis tank, but prediction was poor for variables in the anaerobic tank. The model has limitations in anaerobic reactions, which are basically due to model kinetic parameters unspecific to sugar factory wastewater. © 2012 Desalination Publications. All rights reserved.en_US
dc.description.sponsorshipThe authors would like to express their gratitude to Turkish Sugar Factories Cooperation and Sugar Institute for financial support and permission to use the plant data in this study. This study has also been supported by the Project Management Unit of Akdeniz University, Turkey.en_US
dc.identifier.doi10.1080/19443994.2012.671155
dc.identifier.endpage128en_US
dc.identifier.issn1944-3994
dc.identifier.issue01.Junen_US
dc.identifier.scopus2-s2.0-85025367140en_US
dc.identifier.scopusqualityQ3en_US
dc.identifier.startpage118en_US
dc.identifier.urihttps://dx.doi.org/10.1080/19443994.2012.671155
dc.identifier.urihttps://hdl.handle.net/20.500.12415/7893
dc.identifier.volume40en_US
dc.indekslendigikaynakScopus
dc.language.isoenen_US
dc.publisherTaylor and Francis Inc.en_US
dc.relation.ispartofDesalination and Water Treatmenten_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.snmzKY00625
dc.subjectAnaerobic treatmenten_US
dc.subjectKinetic modelingen_US
dc.subjectSugar industryen_US
dc.titleA simplified kinetic model for a full scale anaerobic wastewater treatment plant of a sugar factory under unsteady conditionsen_US
dc.typeArticle
dspace.entity.typePublication

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