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dc.contributor.authorRahma, Fadilla Noor
dc.contributor.authorLi, Tian
dc.contributor.authorKhalil, Roger Antoine
dc.contributor.authorTran, Quang Khanh
dc.date.accessioned2024-02-22T13:52:26Z
dc.date.available2024-02-22T13:52:26Z
dc.date.created2023-12-14T14:58:41Z
dc.date.issued2023
dc.identifier.citationChemical Engineering Transactions. 2023, 105 217-222.en_US
dc.identifier.issn1974-9791
dc.identifier.urihttps://hdl.handle.net/11250/3119417
dc.description.abstractIn this work, effect of process parameters on hydrothermal gasification (HTG) of biogas digestate are thermodynamically investigated using a Matlab-based code, which is capable of modelling the effects of the feedstock’s inorganic contents and elements. The effects of temperature (400-600 oC), pressure (250-300 bar), and feed concentration (10-40 wt%) towards the producer gas yield and composition are evaluated while considering the influence of inorganic components in the feedstock. The result shows that temperature and feed concentration play significant roles in determining producer gas composition and yield, whereas pressure only has little influence. Hydrogen production is favored by higher temperature, lower pressure, and lower feed concentration. It was also observed that the presence of inorganic components in the feedstock reduces the production of CO2, while H2 and CH4 is increased. The result of this study is essential in the future development of biogas digestate HTG.en_US
dc.description.abstractHydrothermal Gasification of Biogas Digestate: a Parametric Study Using a Matlab-based Codeen_US
dc.language.isoengen_US
dc.publisherAIDICen_US
dc.titleHydrothermal Gasification of Biogas Digestate: a Parametric Study Using a Matlab-based Codeen_US
dc.title.alternativeHydrothermal Gasification of Biogas Digestate: a Parametric Study Using a Matlab-based Codeen_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionpublishedVersionen_US
dc.rights.holderAIDICen_US
dc.source.pagenumber217-222en_US
dc.source.volume105en_US
dc.source.journalChemical Engineering Transactionsen_US
dc.identifier.doi10.3303/CET23105037
dc.identifier.cristin2213751
dc.relation.projectNorges forskningsråd: 319723en_US
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode1


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