Please use this identifier to cite or link to this item: http://hdl.handle.net/10397/103272
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dc.contributorDepartment of Building and Real Estate-
dc.creatorXu, Qen_US
dc.creatorNi, Men_US
dc.date.accessioned2023-12-11T00:32:50Z-
dc.date.available2023-12-11T00:32:50Z-
dc.identifier.issn0363-907Xen_US
dc.identifier.urihttp://hdl.handle.net/10397/103272-
dc.language.isoenen_US
dc.publisherJohn Wiley & Sons Ltd.en_US
dc.rights© 2020 John Wiley & Sons, Ltd.en_US
dc.rightsThis is the peer reviewed version of the following article: Xu, Q, Ni, M. Modelling of high temperature direct methanol solid oxide fuel cells. Int J Energy Res. 2021; 45(2): 3097–3112, which has been published in final form at https://doi.org/10.1002/er.6003. This article may be used for non-commercial purposes in accordance with Wiley Terms and Conditions for Use of Self-Archived Versions. This article may not be enhanced, enriched or otherwise transformed into a derivative work, without express permission from Wiley or by statutory rights under applicable legislation. Copyright notices must not be removed, obscured or modified. The article must be linked to Wiley’s version of record on Wiley Online Library and any embedding, framing or otherwise making available the article or pages thereof by third parties from platforms, services and websites other than Wiley Online Library must be prohibited.en_US
dc.subjectDirect internal reformingen_US
dc.subjectMethanol fuelen_US
dc.subjectModellingen_US
dc.subjectSolid oxide fuel cellen_US
dc.subjectWater gas shift reactionen_US
dc.titleModelling of high temperature direct methanol solid oxide fuel cellsen_US
dc.typeJournal/Magazine Articleen_US
dc.identifier.spage3097en_US
dc.identifier.epage3112en_US
dc.identifier.volume45en_US
dc.identifier.issue2en_US
dc.identifier.doi10.1002/er.6003en_US
dcterms.abstractMethanol is a promising fuel for solid oxide fuel cells (SOFCs). A 2D numerical model is developed to study a tubular direct methanol SOFC. The model fully considers the methanol decomposition reaction and water gas shift reaction in the anode, the electrochemical oxidations of H2 and CO, fluid flow and mass transfer in the cell. The model is validated by the direct methanol SOFC experiment. At a temperature of 1073 K, a peak power density of 1.2 W cm−2 is achieved, which is much higher than room temperature direct methanol fuel cells (typically less than 0.1 W cm−2). Subsequent parametric simulations are conducted to understand the effects of operating and structural parameters on the SOFC performance, such as temperature, potential, anode thickness and cell length. Increasing the temperature enhances chemical/electrochemical reaction rates and ion conduction, leading to improved cell performance. Increasing the anode thickness improves methanol conversion and increases the average current density to some extent. For comparison, a longer cell can also improve methanol conversion but decreases the average cell current density. The results form a basis for subsequent performance enhancement of direct methanol SOFC by optimization of the cell structure and operating parameters.-
dcterms.accessRightsopen accessen_US
dcterms.bibliographicCitationInternational journal of energy research, Feb. 2021, v. 45, no. 2, p. 3097-3112en_US
dcterms.isPartOfInternational journal of energy researchen_US
dcterms.issued2021-02-
dc.identifier.scopus2-s2.0-85092113937-
dc.identifier.eissn1099-114Xen_US
dc.description.validate202312 bcch-
dc.description.oaAccepted Manuscripten_US
dc.identifier.FolderNumberBRE-0441-
dc.description.fundingSourceRGCen_US
dc.description.pubStatusPublisheden_US
dc.identifier.OPUS38878510-
dc.description.oaCategoryGreen (AAM)en_US
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