Please use this identifier to cite or link to this item: http://hdl.handle.net/10397/97569
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dc.contributorDepartment of Building and Real Estateen_US
dc.creatorZhang, Jen_US
dc.creatorZhang, Cen_US
dc.creatorLi, Jen_US
dc.creatorDeng, Ben_US
dc.creatorFan, Men_US
dc.creatorNi, Men_US
dc.creatorMao, Zen_US
dc.creatorYuan, Hen_US
dc.date.accessioned2023-03-06T01:20:11Z-
dc.date.available2023-03-06T01:20:11Z-
dc.identifier.issn0960-1481en_US
dc.identifier.urihttp://hdl.handle.net/10397/97569-
dc.language.isoenen_US
dc.publisherPergamon Pressen_US
dc.rights© 2021 Elsevier Ltd. All rights reserved.en_US
dc.rights© 2021. This manuscript version is made available under the CC-BY-NC-ND 4.0 license http://creativecommons.org/licenses/by-nc-nd/4.0/.en_US
dc.rightsThe following publication Zhang, J., Zhang, C., Li, J., Deng, B., Fan, M., Ni, M., Mao, Z., & Yuan, H. (2021). Multi-perspective analysis of CO poisoning in high-temperature proton exchange membrane fuel cell stack via numerical investigation. Renewable Energy, 180, 313-328 is available at https://dx.doi.org/10.1016/j.renene.2021.08.089.en_US
dc.subjectAnodic kinetic parametersen_US
dc.subjectCO poisoningen_US
dc.subjectH2 and CO coverageen_US
dc.subjectHT-PEMFC stacken_US
dc.subjectNumerical modelen_US
dc.titleMulti-perspective analysis of CO poisoning in high-temperature proton exchange membrane fuel cell stack via numerical investigationen_US
dc.typeJournal/Magazine Articleen_US
dc.identifier.spage313en_US
dc.identifier.epage328en_US
dc.identifier.volume180en_US
dc.identifier.doi10.1016/j.renene.2021.08.089en_US
dcterms.abstractTo comprehensively understand the CO poisoning effect on high-temperature PEMFC stack (HT-PEMFCs), a 3-D numerical HT-PEMFCs model is developed. The crucial anodic kinetic parameters are obtained from experimental data to improve the accuracy of the model. Then, multi-perspective analysis is conducted on different HT-PEMFC stacks with 1, 3, and 5 cells working at 160 °C with 3 mol% CO in H2. Besides, parametric simulations are conducted on the three-cell stack. It is found that the CO and H2 coverage varies between cells in the stack due to the temperature distribution difference, and the stack with more cells as well as the middle-cell of multi-cell stack have better performance, higher H2 coverage, lower CO coverage due to higher internal temperature. However, too high local temperature not only reduce the CO coverage but reduce the H2 coverage and increase the anode overpotential. The resistance to CO poisoning can be improved by increasing operating temperature, but when CO2 and water vapor are introduced into the anode, the H2 coverage decreases and the CO coverage increases due to the decrease of H2 concentration. The study clearly demonstrated that high performance and high CO resistance can be achieved by carefully regulating the operating conditions.en_US
dcterms.accessRightsopen accessen_US
dcterms.bibliographicCitationRenewable energy, Dec. 2021, v. 180, p. 313-328en_US
dcterms.isPartOfRenewable energyen_US
dcterms.issued2021-12-
dc.identifier.scopus2-s2.0-85113820492-
dc.identifier.eissn1879-0682en_US
dc.description.validate202303 bcwwen_US
dc.description.oaAccepted Manuscripten_US
dc.identifier.FolderNumberBRE-0021-
dc.description.fundingSourceRGCen_US
dc.description.pubStatusPublisheden_US
dc.identifier.OPUS55585755-
dc.description.oaCategoryGreen (AAM)en_US
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