Please use this identifier to cite or link to this item: http://hdl.handle.net/10397/103250
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dc.contributorDepartment of Building and Real Estate-
dc.creatorZhang, Jen_US
dc.creatorZhang, Cen_US
dc.creatorHao, Den_US
dc.creatorNi, Men_US
dc.creatorHuang, Sen_US
dc.creatorLiu, Den_US
dc.creatorZheng, Yen_US
dc.date.accessioned2023-12-11T00:32:38Z-
dc.date.available2023-12-11T00:32:38Z-
dc.identifier.issn0360-3199en_US
dc.identifier.urihttp://hdl.handle.net/10397/103250-
dc.language.isoenen_US
dc.publisherElsevier Ltden_US
dc.rights© 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.en_US
dc.rights© 2020. 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 Zhang, J., Zhang, C., Hao, D., Ni, M., Huang, S., Liu, D., & Zheng, Y. (2021). 3D non-isothermal dynamic simulation of high temperature proton exchange membrane fuel cell in the start-up process. International Journal of Hydrogen Energy, 46(2), 2577-2593 is available at https://doi.org/10.1016/j.ijhydene.2020.10.116.en_US
dc.subjectCounter-flowen_US
dc.subjectHT-PEMFCen_US
dc.subjectStart-up processen_US
dc.subjectTemperature distributionen_US
dc.title3D non-isothermal dynamic simulation of high temperature proton exchange membrane fuel cell in the start-up processen_US
dc.typeJournal/Magazine Articleen_US
dc.identifier.spage2577en_US
dc.identifier.epage2593en_US
dc.identifier.volume46en_US
dc.identifier.issue2en_US
dc.identifier.doi10.1016/j.ijhydene.2020.10.116en_US
dcterms.abstractHigh temperature proton exchange membrane fuel cell (HT-PEMFC) with phosphoric acid doped polybenzimidazole (PBI) electrolyte shows multiple advantages over conventional PEMFC working at below 373 K, such as faster electrochemical kinetics, simpler water management, higher carbon monoxide tolerance. However, starting HT-PEMFC from room temperature to the optimal operating temperature range (433.15 K–453.15 K) is still a serious challenge. In present work, the start-up strategy is proposed and evaluated and a three-dimensional non-isothermal dynamic model is developed to investigate start-up time and temperature distribution during the start-up process. The HT-PEMFC is preheated by gas to 393.15 K, followed by discharging a current from the cell for electrochemical heat generation. Firstly, different current loads are applied when the average temperature of membrane reaches 393.15 K. Then, the start-up time and temperature distribution of co-flow and counter-flow are compared at different current loads. Finally, the effect of inlet velocity and temperature on the start-up process are explored in the case of counter-flow. Numerical results clearly show that applied current load is necessary to reduce start-up time and just 0.1 A/cm2 current load can reduce startup time by 45%. It is also found that co-flow takes 18.8% less time than counter-flow to heat membrane temperature to 393.15 K, but the maximum temperature difference of membrane is 39% higher than the counter-flow. Increasing the inlet gas flow velocity and temperature can shorten the start-up time but increases the temperature difference of the membrane.-
dcterms.accessRightsopen accessen_US
dcterms.bibliographicCitationInternational journal of hydrogen energy, 6 Jan. 2021, v. 46, no. 2, p. 2577-2593en_US
dcterms.isPartOfInternational journal of hydrogen energyen_US
dcterms.issued2021-01-06-
dc.identifier.scopus2-s2.0-85095811184-
dc.identifier.eissn1879-3487en_US
dc.description.validate202312 bcch-
dc.description.oaAccepted Manuscripten_US
dc.identifier.FolderNumberBRE-0403-
dc.description.fundingSourceRGCen_US
dc.description.pubStatusPublisheden_US
dc.identifier.OPUS38877861-
dc.description.oaCategoryGreen (AAM)en_US
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