Please use this identifier to cite or link to this item: http://hdl.handle.net/10397/103396
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dc.contributorDepartment of Building and Real Estate-
dc.creatorChen, Ben_US
dc.creatorXu, Hen_US
dc.creatorSun, Qen_US
dc.creatorZhang, Hen_US
dc.creatorTan, Pen_US
dc.creatorCai, Wen_US
dc.creatorHe, Wen_US
dc.creatorNi, Men_US
dc.date.accessioned2023-12-11T00:33:38Z-
dc.date.available2023-12-11T00:33:38Z-
dc.identifier.issn0196-8904en_US
dc.identifier.urihttp://hdl.handle.net/10397/103396-
dc.language.isoenen_US
dc.publisherElsevier Ltden_US
dc.rights© 2018 Elsevier Ltd. All rights reserved.en_US
dc.rights© 2018. This manuscript version is made available under the CC-BY-NC-ND 4.0 license https://creativecommons.org/licenses/by-nc-nd/4.0/en_US
dc.rightsThe following publication Chen, B., Xu, H., Sun, Q., Zhang, H., Tan, P., Cai, W., ... & Ni, M. (2018). Syngas/power cogeneration from proton conducting solid oxide fuel cells assisted by dry methane reforming: A thermal-electrochemical modelling study. Energy Conversion and Management, 167, 37-44 is available at https://doi.org/10.1016/j.enconman.2018.04.078.en_US
dc.subjectCogenerationen_US
dc.subjectDry methane reformingen_US
dc.subjectFinite element modellingen_US
dc.subjectProton conductingen_US
dc.subjectSolid oxide fuel cellsen_US
dc.titleSyngas/power cogeneration from proton conducting solid oxide fuel cells assisted by dry methane reforming : a thermal-electrochemical modelling studyen_US
dc.typeJournal/Magazine Articleen_US
dc.identifier.spage37en_US
dc.identifier.epage44en_US
dc.identifier.volume167en_US
dc.identifier.doi10.1016/j.enconman.2018.04.078en_US
dcterms.abstractA tubular proton conducting solid oxide fuel cell (H-SOFC) integrated with internal dry methane reforming (DMR) layer is numerically studied for power and syngas cogeneration using CO2 and CH4 as fuel by the Finite Element Method. The coupled heat and mass transporting with electrochemical reactions and chemical reactions (DMR, water gas shifting reaction and methane steam reforming) are fully considered. The model is substantially validated with experimental data of DMR catalyst characterization and SOFC button cell electrochemical characterization. The base case analyses are conducted at open circuit voltage (OCV) and 0.7 V of the DMR-SOFC. It is found that the CO2 conversion and CH4 conversion can be increased by 4.8% and 21.6%, respectively, by increasing the operating voltage of DMR-SOFC from OCV to 0.7 V, with the coproduction of electricity (1.5 W). These conversion enhancements were caused by the in-situ integration of the endothermal DMR reaction and exothermal H2 electrochemical oxidation. Effects of operating voltage and inlet flow rate of feeding gas are evaluated. The voltage is suggested to be higher than 0.5 V to avoid large temperature gradient in the reactor. It is also found that conversion ratios of both CH4 and CO2 decrease from over 90% to be below 60% as the fuel flow rate is increased from 40 cm3 min−1 to 80 cm3 min−1.-
dcterms.accessRightsopen accessen_US
dcterms.bibliographicCitationEnergy conversion and management, 1 July 2018, v. 167, p. 37-44en_US
dcterms.isPartOfEnergy conversion and managementen_US
dcterms.issued2018-07-01-
dc.identifier.scopus2-s2.0-85046379516-
dc.identifier.eissn1879-2227en_US
dc.description.validate202312 bcch-
dc.description.oaAccepted Manuscripten_US
dc.identifier.FolderNumberBRE-0763-
dc.description.fundingSourceRGCen_US
dc.description.pubStatusPublisheden_US
dc.identifier.OPUS6837242-
dc.description.oaCategoryGreen (AAM)en_US
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