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Restructuring anaerobic hydrolysis kinetics in plant-wide models for accurate prediction of biogas production

dc.contributor.authorOzyildiz, Goksin
dc.contributor.authorZengin, Gulsum Emel
dc.contributor.authorGüven, Didem
dc.contributor.authorCokgor, Emine
dc.contributor.authorÖzdemir, Özgür
dc.contributor.authorHauduc, Hélène
dc.contributor.authorTakács, Imre
dc.contributor.authorInsel, Güçlü
dc.contributor.ituauthorZengin, Balcı Gülsüm Emel
dc.contributor.ituauthorÇokgör, Emine
dc.contributor.ituauthorİnsel, Hayrettin Güçlü
dc.date.accessioned2026-01-26T00:21:09Z
dc.date.issued2023-10-01
dc.description.abstractIn this study, the effect of anaerobic hydrolysis rate on biogas production was investigated with mesophilic digesters in seven large-scale wastewater treatment plants. A linear correlation was determined between the percentage of primary sludge mass in the total sludge fed to the digester and the overall anaerobic hydrolysis rate. The anaerobic hydrolysis rate of primary sludge was determined to be three times higher than that of biological sludge. The reduction factors for anaerobic hydrolysis (ηHYD,ana) were identified in the range of 0.11-0.30 which is lower compared to the recommended range (0.30-0.50) given in the literature. This study proposes a new model approach where anaerobic degradation kinetics of influent originated (XB) and decay originated (XB,E) particulate biodegradable organics are separated. Current plant-wide models with a single kinetic expression required recalibration of the model for calculating biogas flowrate for each treatment facility with different primary and secondary sludge ratios fed to the digesters. The new model structure is able to predict biogas production of all wastewater treatment plants without any recalibration effort by segregating degradation kinetics of two particulate biodegradable organic fractions (XB, XB,E).
dc.description.urihttps://doi.org/10.1016/j.watres.2023.120620
dc.description.urihttps://pubmed.ncbi.nlm.nih.gov/37717326
dc.identifier.doi10.1016/j.watres.2023.120620
dc.identifier.issn0043-1354
dc.identifier.openairedoi_dedup___::ad0c18722a53a06aecaed1045a6142ff
dc.identifier.orcid0000-0003-1423-9234
dc.identifier.orcid0000-0002-6475-9062
dc.identifier.orcid0000-0002-4904-6056
dc.identifier.orcid0000-0002-0573-9221
dc.identifier.orcid0000-0001-6597-2693
dc.identifier.startpage120620
dc.identifier.urihttps://hdl.handle.net/11527/54157
dc.identifier.volume245
dc.language.isoeng
dc.publisherElsevier BV
dc.relation.ispartofWater Research
dc.rightsCLOSED
dc.sdg.typeGoal 7: Affordable and Clean Energy
dc.sdg.typeGoal 6: Clean Water and Sanitation
dc.titleRestructuring anaerobic hydrolysis kinetics in plant-wide models for accurate prediction of biogas production
dc.typeArticle
dspace.entity.typePublication
person.identifier.orcid0000-0002-6475-9062
person.identifier.orcid0000-0002-4904-6056
person.identifier.orcid0000-0001-6597-2693

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