Please use this identifier to cite or link to this item: http://hdl.handle.net/10397/6503
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dc.contributorDepartment of Building and Real Estate-
dc.creatorNi, M-
dc.date.accessioned2014-12-11T08:25:24Z-
dc.date.available2014-12-11T08:25:24Z-
dc.identifier.issn0360-3199-
dc.identifier.urihttp://hdl.handle.net/10397/6503-
dc.language.isoenen_US
dc.publisherPergamon Pressen_US
dc.rights© 2010 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.en_US
dc.rightsPosted with permission of Professor T. Nejat Veziroglu.en_US
dc.subjectSolid oxide fuel cellsen_US
dc.subjectHeat transferen_US
dc.subjectElectrochemistryen_US
dc.subjectPorous mediaen_US
dc.subjectAmmonia thermal decompositionen_US
dc.titleThermo-electrochemical modeling of ammonia-fueled solid oxide fuel cells considering ammonia thermal decomposition in the anodeen_US
dc.typeJournal/Magazine Articleen_US
dc.identifier.spage3153-
dc.identifier.epage3166-
dc.identifier.volume36-
dc.identifier.issue4-
dc.identifier.doi10.1016/j.ijhydene.2010.11.100-
dcterms.abstractAmmonia (NH₃) is a promising hydrogen carrier and a possible fuel for use in Solid Oxide Fuel Cells (SOFCs). In this study, a 2D thermo-electrochemical model is developed to investigate the heat/mass transfer, chemical (ammonia thermal decomposition) and electrochemical reactions in a planar SOFC running on ammonia. The model integrates three sub-models: (1) an electrochemical model relating the current density–voltage characteristics; (2) a chemical model calculating the rate of ammonia thermal decomposition reaction; (3) a 2D computational fluid dynamics (CFD) model that simulates the heat and mass transfer phenomena. Simulations are conducted to study the complicated physical–chemical processes in NH₃-fueled SOFCs. It is found that increasing the inlet temperature of NH₃-fueled SOFC is favorable for a higher electric output, but the temperature gradient in the SOFC is considerably higher, particularly near the inlet of the SOFC. The effects of operating potential and inlet gas velocity on NH3-fueled SOFC performance are investigated. It is found that an increase in inlet gas velocity from 1 m s⁻¹ to 10 m s⁻¹ slightly decreases the SOFC performance and does not affect the temperature field significantly. For comparison, decreasing the gas velocity to 0.2 m s⁻¹ is more effective to reduce the temperature gradient in SOFC.-
dcterms.accessRightsopen accessen_US
dcterms.bibliographicCitationInternational journal of hydrogen energy, Feb. 2011, v. 36, no. 4, p. 3153-3166-
dcterms.isPartOfInternational journal of hydrogen energy-
dcterms.issued2011-02-
dc.identifier.isiWOS:000288772900041-
dc.identifier.scopus2-s2.0-79951581432-
dc.identifier.eissn1879-3487-
dc.identifier.rosgroupidr53888-
dc.description.ros2010-2011 > Academic research: refereed > Publication in refereed journal-
dc.description.oaVersion of Recorden_US
dc.identifier.FolderNumberOA_IR/PIRAen_US
dc.description.pubStatusPublisheden_US
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