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- Publisher Website: 10.1016/j.ijhydene.2008.07.021
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Article: Mathematical modeling of ammonia-fed solid oxide fuel cells with different electrolytes
Title | Mathematical modeling of ammonia-fed solid oxide fuel cells with different electrolytes | ||||
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Authors | |||||
Keywords | Ammonia fuel Electrochemical modeling Multi-component mass transfer Oxygen-ion conductors Porous media Proton-conducting ceramics Solid oxide fuel cell (SOFC) | ||||
Issue Date | 2008 | ||||
Publisher | Pergamon. The Journal's web site is located at http://www.elsevier.com/locate/ijhydene | ||||
Citation | International Journal Of Hydrogen Energy, 2008, v. 33 n. 20, p. 5765-5772 How to Cite? | ||||
Abstract | An electrochemical model was developed to study the ammonia (NH3)-fed solid oxide fuel cells with proton-conducting electrolyte (SOFC-H) and oxygen ion-conducting electrolyte (SOFC-O). Different from previous thermodynamic analysis, the present study reveals that the actual performance of the NH3-fed SOFC-H is considerably lower than the SOFC-O, mainly due to higher ohmic overpotential of the SOFC-H electrolyte. More analyses have been performed to study the separate overpotentials of the NH3-fed SOFC-H and SOFC-O. Compared with the NH3-fed SOFC-H, the SOFC-O has higher anode concentration overpotential and lower cathode concentration overpotential. The effects of temperature and electrode porosity on concentration overpotentials have also been studied in order to identify possible methods for improvement of SOFC performance. This study reveals that the use of different electrolytes not only causes different ion conduction characteristics at the electrolyte, but also significantly influences the concentration overpotentials at the electrodes. The model developed in this article can be extended to 2D and 3D models for further design optimization. © 2008 International Association for Hydrogen Energy. | ||||
Persistent Identifier | http://hdl.handle.net/10722/59058 | ||||
ISSN | 2023 Impact Factor: 8.1 2023 SCImago Journal Rankings: 1.513 | ||||
ISI Accession Number ID |
Funding Information: The authors thank the financial support by the CRCG of the University of Hong Kong. They also thank Prof. G.Y. Meng (University of Science and Technology of China), Prof. S.H. Chan (Nanyang Technological University, Singapore) and Prof. A.K. Demin (institute of High Temperature Electrochemistry, Russia) for their discussions and suggestions in SOFC research. | ||||
References |
DC Field | Value | Language |
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dc.contributor.author | Ni, M | en_HK |
dc.contributor.author | Leung, DYC | en_HK |
dc.contributor.author | Leung, MKH | en_HK |
dc.date.accessioned | 2010-05-31T03:42:10Z | - |
dc.date.available | 2010-05-31T03:42:10Z | - |
dc.date.issued | 2008 | en_HK |
dc.identifier.citation | International Journal Of Hydrogen Energy, 2008, v. 33 n. 20, p. 5765-5772 | en_HK |
dc.identifier.issn | 0360-3199 | en_HK |
dc.identifier.uri | http://hdl.handle.net/10722/59058 | - |
dc.description.abstract | An electrochemical model was developed to study the ammonia (NH3)-fed solid oxide fuel cells with proton-conducting electrolyte (SOFC-H) and oxygen ion-conducting electrolyte (SOFC-O). Different from previous thermodynamic analysis, the present study reveals that the actual performance of the NH3-fed SOFC-H is considerably lower than the SOFC-O, mainly due to higher ohmic overpotential of the SOFC-H electrolyte. More analyses have been performed to study the separate overpotentials of the NH3-fed SOFC-H and SOFC-O. Compared with the NH3-fed SOFC-H, the SOFC-O has higher anode concentration overpotential and lower cathode concentration overpotential. The effects of temperature and electrode porosity on concentration overpotentials have also been studied in order to identify possible methods for improvement of SOFC performance. This study reveals that the use of different electrolytes not only causes different ion conduction characteristics at the electrolyte, but also significantly influences the concentration overpotentials at the electrodes. The model developed in this article can be extended to 2D and 3D models for further design optimization. © 2008 International Association for Hydrogen Energy. | en_HK |
dc.language | eng | en_HK |
dc.publisher | Pergamon. The Journal's web site is located at http://www.elsevier.com/locate/ijhydene | en_HK |
dc.relation.ispartof | International Journal of Hydrogen Energy | en_HK |
dc.subject | Ammonia fuel | en_HK |
dc.subject | Electrochemical modeling | en_HK |
dc.subject | Multi-component mass transfer | en_HK |
dc.subject | Oxygen-ion conductors | en_HK |
dc.subject | Porous media | en_HK |
dc.subject | Proton-conducting ceramics | en_HK |
dc.subject | Solid oxide fuel cell (SOFC) | en_HK |
dc.title | Mathematical modeling of ammonia-fed solid oxide fuel cells with different electrolytes | en_HK |
dc.type | Article | en_HK |
dc.identifier.openurl | http://library.hku.hk:4550/resserv?sid=HKU:IR&issn=0360-3199&volume=33&spage=5765&epage=5772&date=2008&atitle=Mathematical+modeling+of+ammonia-fed+solid+oxide+fuel+cells+with+different+electrolytes | en_HK |
dc.identifier.email | Leung, DYC: ycleung@hku.hk | en_HK |
dc.identifier.email | Leung, MKH: | en_HK |
dc.identifier.authority | Leung, DYC=rp00149 | en_HK |
dc.identifier.authority | Leung, MKH=rp00148 | en_HK |
dc.description.nature | link_to_subscribed_fulltext | - |
dc.identifier.doi | 10.1016/j.ijhydene.2008.07.021 | en_HK |
dc.identifier.scopus | eid_2-s2.0-53449092025 | en_HK |
dc.identifier.hkuros | 153391 | en_HK |
dc.relation.references | http://www.scopus.com/mlt/select.url?eid=2-s2.0-53449092025&selection=ref&src=s&origin=recordpage | en_HK |
dc.identifier.volume | 33 | en_HK |
dc.identifier.issue | 20 | en_HK |
dc.identifier.spage | 5765 | en_HK |
dc.identifier.epage | 5772 | en_HK |
dc.identifier.isi | WOS:000261009000058 | - |
dc.publisher.place | United Kingdom | en_HK |
dc.identifier.scopusauthorid | Ni, M=9268339800 | en_HK |
dc.identifier.scopusauthorid | Leung, DYC=7203002484 | en_HK |
dc.identifier.scopusauthorid | Leung, MKH=8862966600 | en_HK |
dc.identifier.issnl | 0360-3199 | - |