Please use this identifier to cite or link to this item: http://hdl.handle.net/10397/95899
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dc.contributorDepartment of Building and Real Estateen_US
dc.creatorXu, Hen_US
dc.creatorChen, Ben_US
dc.creatorTan, Pen_US
dc.creatorCai, Wen_US
dc.creatorWu, Yen_US
dc.creatorZhang, Hen_US
dc.creatorNi, Men_US
dc.date.accessioned2022-10-26T01:09:20Z-
dc.date.available2022-10-26T01:09:20Z-
dc.identifier.issn0306-2619en_US
dc.identifier.urihttp://hdl.handle.net/10397/95899-
dc.language.isoenen_US
dc.publisherPergamon Pressen_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 Xu, H., Chen, B., Tan, P., Cai, W., Wu, Y., Zhang, H., & Ni, M. (2018). A feasible way to handle the heat management of direct carbon solid oxide fuel cells. Applied energy, 226, 881-890 is available at https://doi.org/10.1016/j.apenergy.2018.06.039.en_US
dc.subjectCarbon gasificationen_US
dc.subjectHeat managementen_US
dc.subjectPerformance improvementen_US
dc.subjectSolid oxide fuel cellen_US
dc.subjectVacuum thermionic generatoren_US
dc.titleA feasible way to handle the heat management of direct carbon solid oxide fuel cellsen_US
dc.typeJournal/Magazine Articleen_US
dc.identifier.spage881en_US
dc.identifier.epage890en_US
dc.identifier.volume226en_US
dc.identifier.doi10.1016/j.apenergy.2018.06.039en_US
dcterms.abstractA novel integrated system consisting of an external heat source, a direct carbon solid oxide fuel cell (DC-SOFC), a vacuum thermionic generator (VTIG) and a regenerator is proposed to handle the heat management of the DC-SOFC. The electrochemical/chemical reactions, ionic/electronic charge transport, mass/momentum transport and heat transfer are fully considered in the 2D tubular DC-SOFC model, which shows that the overall heat released in the cell is always different from the heat required by the internal Boudouard reaction. Three different operation strategies of the proposed system are presented, and accordingly, analytical expressions for the overall power output and efficiency for the proposed system are specified. The results show that the VTIG could effectively recover the waste heat for additional power production at a large operating current density, and the maximum power density and efficiency of the proposed system could reach more than 8100 W m−2 and 60% at 30,000 A m−2 and 1173 K, respectively. The effects of the operating current density, the operating temperature and the distance between the carbon layer and anode of the DC-SOFC, and the size, anode temperature and work function of the VTIG on the performance of the proposed system are discussed through comprehensive parametric studies.en_US
dcterms.accessRightsopen accessen_US
dcterms.bibliographicCitationApplied energy, 15 Sept. 2018, v. 226, p. 881-890en_US
dcterms.isPartOfApplied energyen_US
dcterms.issued2018-09-
dc.identifier.scopus2-s2.0-85048383269-
dc.identifier.eissn1872-9118en_US
dc.description.validate202210 bcwwen_US
dc.description.oaAccepted Manuscripten_US
dc.identifier.FolderNumberBRE-0732-
dc.description.fundingSourceRGCen_US
dc.description.pubStatusPublisheden_US
dc.identifier.OPUS6845294-
dc.description.oaCategoryGreen (AAM)en_US
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