Please use this identifier to cite or link to this item: http://hdl.handle.net/10397/113912
DC FieldValueLanguage
dc.contributorDepartment of Mechanical Engineeringen_US
dc.creatorLiu, Yen_US
dc.creatorPan, Zen_US
dc.creatorHuo, Xen_US
dc.creatorLi, Wen_US
dc.creatorShi, Xen_US
dc.creatorChen, Ren_US
dc.creatorAn, Len_US
dc.date.accessioned2025-06-27T09:30:32Z-
dc.date.available2025-06-27T09:30:32Z-
dc.identifier.issn0360-3199en_US
dc.identifier.urihttp://hdl.handle.net/10397/113912-
dc.language.isoenen_US
dc.publisherPergamon Pressen_US
dc.subjectAmmoniaen_US
dc.subjectBubble dynamicsen_US
dc.subjectFlow fieldsen_US
dc.subjectFuel cellsen_US
dc.subjectTwo-phase flowen_US
dc.titleTwo-phase flow visualization in direct ammonia fuel cellsen_US
dc.typeJournal/Magazine Articleen_US
dc.identifier.spage159en_US
dc.identifier.epage169en_US
dc.identifier.volume70en_US
dc.identifier.doi10.1016/j.ijhydene.2024.05.158en_US
dcterms.abstractIn this work, the two-phase flow occurring in a direct ammonia fuel cell is visualized to understand the interactions between the complex physico-chemical processes involving in fuel cells. Experimental observations indicate that the appearance, growth, coalescence, detachment and sweeping processes of nitrogen bubbles occur periodically. Besides, the effect of operating conditions on the behavior of two-phase flow as well as cell performance is explored. Experimental results demonstrate that numerous nitrogen gas slugs are generated in the anode flow channel when the fuel flow rate is lower than 1.0 mL min−1, which seriously blocks the transport of NH3 and OH− to the anode catalyst layer. At an operating temperature of 95 °C, the flow channels are almost completely occupied by gases (a mixture of ammonia, nitrogen, and water), even under open-circuit conditions (a mixture of ammonia and water). In addition, the effects of using parallel and serpentine flow fields on the behaviour and flow patterns of two-phase flows are explored. Experimental results reveal that the parallel flow field is prone to clogging local flow channels by slugs. Moreover, the removal frequency of bubbles in the parallel design is significantly slower than that in the serpentine one.en_US
dcterms.accessRightsembargoed accessen_US
dcterms.bibliographicCitationInternational journal of hydrogen energy, 12 June 2024, v. 70, p. 159-169en_US
dcterms.isPartOfInternational journal of hydrogen energyen_US
dcterms.issued2024-06-12-
dc.identifier.scopus2-s2.0-85193227728-
dc.identifier.eissn1879-3487en_US
dc.description.validate202506 bcchen_US
dc.description.oaNot applicableen_US
dc.identifier.FolderNumbera3814c-
dc.identifier.SubFormID51208-
dc.description.fundingSourceOthersen_US
dc.description.fundingTextChongqing University; National Natural Science Foundation of China; Shenzhen Science and Technology Innovation Commissionen_US
dc.description.pubStatusPublisheden_US
dc.date.embargo2026-06-12en_US
dc.description.oaCategoryGreen (AAM)en_US
Appears in Collections:Journal/Magazine Article
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Embargo End Date 2026-06-12
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