Please use this identifier to cite or link to this item: http://hdl.handle.net/10397/95905
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dc.contributorDepartment of Building and Real Estateen_US
dc.contributorDepartment of Building and Real Estate-
dc.contributorResearch Institute for Sustainable Urban Development-
dc.creatorXu, Hen_US
dc.creatorChen, Ben_US
dc.creatorZhang, Hen_US
dc.creatorSun, Qen_US
dc.creatorYang, Gen_US
dc.creatorNi, Men_US
dc.date.accessioned2022-10-26T01:09:23Z-
dc.date.available2022-10-26T01:09:23Z-
dc.identifier.issn0360-3199en_US
dc.identifier.urihttp://hdl.handle.net/10397/95905-
dc.language.isoenen_US
dc.publisherPergamon Pressen_US
dc.rights© 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.en_US
dc.rights© 2017. 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 Xu, H., Chen, B., Zhang, H., Sun, Q., Yang, G., & Ni, M. (2017). Modeling of direct carbon solid oxide fuel cells with H2O and CO2 as gasification agents. International Journal of Hydrogen Energy, 42(23), 15641-15651 is available at https://doi.org/10.1016/j.ijhydene.2017.05.075.en_US
dc.subjectMathematical modelingen_US
dc.subjectSolid oxide fuel cell (SOFC)en_US
dc.subjectSteam gasification of carbonen_US
dc.titleModeling of direct carbon solid oxide fuel cells with H2O and CO2 as gasification agentsen_US
dc.typeJournal/Magazine Articleen_US
dc.identifier.spage15641en_US
dc.identifier.epage15651en_US
dc.identifier.volume42en_US
dc.identifier.issue23en_US
dc.identifier.doi10.1016/j.ijhydene.2017.05.075en_US
dcterms.abstractIn this paper, 2D models for direct carbon solid oxide fuel cells (DC-SOFCs) with H2O and CO2 as agents for carbon gasification are developed. The simulation results are compared with experimental data and good agreement is obtained. The performance of DC-SOFCs with two agents is compared at different operating potential, temperature and anode inlet gas flow rate. It is found that the H2O assisted DC-SOFC performs significantly better than the CO2-assisted DC-SOFC, indicating the suitability of H2O for DC-SOFCs. It is also found that a higher temperature could greatly improve the performance of both kinds of DC-SOFCs. At a temperature of 1000 K and operating voltage of 0.5 V, the current density from the CO2-assisted DC-SOFC is close to 0 while it is still above 1000 A m−2 from the H2O-assisted DC-SOFC, indicating the possibility of operating the H2O assisted DC-SOFC at reduced temperature. It is found that the anode gas flow rate does not significantly affect the performance of DC-SOFC. To further improve the performance of H2O assisted DC-SOFCs, developing suitable catalysts for enhancing carbon gasification kinetics could be a good strategy. The results of this study form a solid foundation to understand H2O assisted DC-SOFCs.en_US
dcterms.accessRightsopen accessen_US
dcterms.bibliographicCitationInternational journal of hydrogen energy, 8 June 2017, v. 42, no. 23, p. 15641-15651en_US
dcterms.isPartOfInternational journal of hydrogen energyen_US
dcterms.issued2017-06-08-
dc.identifier.scopus2-s2.0-85019663399-
dc.identifier.eissn1879-3487en_US
dc.description.validate202210 bcwwen_US
dc.description.oaAccepted Manuscripten_US
dc.identifier.FolderNumberBRE-0939-
dc.description.fundingSourceRGCen_US
dc.description.pubStatusPublisheden_US
dc.identifier.OPUS6747802-
dc.description.oaCategoryGreen (AAM)en_US
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