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Article: An improved electrochemical model for the NH3 fed proton conducting solid oxide fuel cells at intermediate temperatures
Title | An improved electrochemical model for the NH3 fed proton conducting solid oxide fuel cells at intermediate temperatures | ||||
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Authors | |||||
Keywords | Ammonia catalytic decomposition Ammonia fuel Electrochemical model Mass transfer Proton conducting ceramics Solid oxide fuel cell (SOFC) | ||||
Issue Date | 2008 | ||||
Publisher | Elsevier SA. The Journal's web site is located at http://www.elsevier.com/locate/jpowsour | ||||
Citation | Journal Of Power Sources, 2008, v. 185 n. 1, p. 233-240 How to Cite? | ||||
Abstract | An improved electrochemical model is developed to study the ammonia fed solid oxide fuel cell based on proton conducting electrolyte (SOFC-H). Including the chemical reaction kinetics of NH3 catalytic thermal decomposition, the present model can be used to predict the performance of the NH3 fed SOFC-H at an intermediate temperature (i.e. 773 K). Comparison between the simulation results using the present model and experimental data from literature validates the accuracy of this model. Parametrical analyses reveal that at a high operating temperature (i.e. 1073 K), the NH3 fuel is completely decomposed to H2 and N2 within a very thin layer (30 μm) near the anode surface of an SOFC-H. It is also found that operating the NH3 fed SOFC-H at an intermediate temperature of 773 K is feasible due to sufficiently high rate of NH3 decomposition. However, further decreasing the temperature to 673 K is not recommended as less than 10% NH3 fuel can be decomposed to H2 and N2 in the SOFC-H. The effects of current density and electrode microstructure on the performance of the NH3 fed SOFC-H are also studied. It is found that increasing electrode porosity and pore size is beneficial to increase the partial pressure of H2 at the anode-electrolyte interface. The model developed in this paper can be extended to 2D or 3D models to study practical tubular or planar SOFCs. © 2008 Elsevier B.V. All rights reserved. | ||||
Persistent Identifier | http://hdl.handle.net/10722/59003 | ||||
ISSN | 2023 Impact Factor: 8.1 2023 SCImago Journal Rankings: 1.857 | ||||
ISI Accession Number ID |
Funding Information: The authors would like to thank the financial support by the CRCG of the University of Hong Kong. The authors also thank Prof. G.Y. Meng (University of Science and Technology of China), Prof. A.K. Demin (institute of High Temperature Electrochemistry, Russia), and Prof. S.H. Chan (Nanyang Technological University, Singapore) for their discussions and suggestions in our SOFC research. | ||||
References |
DC Field | Value | Language |
---|---|---|
dc.contributor.author | Ni, M | en_HK |
dc.contributor.author | Leung, DYC | en_HK |
dc.contributor.author | Leung, MKH | en_HK |
dc.date.accessioned | 2010-05-31T03:41:14Z | - |
dc.date.available | 2010-05-31T03:41:14Z | - |
dc.date.issued | 2008 | en_HK |
dc.identifier.citation | Journal Of Power Sources, 2008, v. 185 n. 1, p. 233-240 | en_HK |
dc.identifier.issn | 0378-7753 | en_HK |
dc.identifier.uri | http://hdl.handle.net/10722/59003 | - |
dc.description.abstract | An improved electrochemical model is developed to study the ammonia fed solid oxide fuel cell based on proton conducting electrolyte (SOFC-H). Including the chemical reaction kinetics of NH3 catalytic thermal decomposition, the present model can be used to predict the performance of the NH3 fed SOFC-H at an intermediate temperature (i.e. 773 K). Comparison between the simulation results using the present model and experimental data from literature validates the accuracy of this model. Parametrical analyses reveal that at a high operating temperature (i.e. 1073 K), the NH3 fuel is completely decomposed to H2 and N2 within a very thin layer (30 μm) near the anode surface of an SOFC-H. It is also found that operating the NH3 fed SOFC-H at an intermediate temperature of 773 K is feasible due to sufficiently high rate of NH3 decomposition. However, further decreasing the temperature to 673 K is not recommended as less than 10% NH3 fuel can be decomposed to H2 and N2 in the SOFC-H. The effects of current density and electrode microstructure on the performance of the NH3 fed SOFC-H are also studied. It is found that increasing electrode porosity and pore size is beneficial to increase the partial pressure of H2 at the anode-electrolyte interface. The model developed in this paper can be extended to 2D or 3D models to study practical tubular or planar SOFCs. © 2008 Elsevier B.V. All rights reserved. | en_HK |
dc.language | eng | en_HK |
dc.publisher | Elsevier SA. The Journal's web site is located at http://www.elsevier.com/locate/jpowsour | en_HK |
dc.relation.ispartof | Journal of Power Sources | en_HK |
dc.subject | Ammonia catalytic decomposition | en_HK |
dc.subject | Ammonia fuel | en_HK |
dc.subject | Electrochemical model | en_HK |
dc.subject | Mass transfer | en_HK |
dc.subject | Proton conducting ceramics | en_HK |
dc.subject | Solid oxide fuel cell (SOFC) | en_HK |
dc.title | An improved electrochemical model for the NH3 fed proton conducting solid oxide fuel cells at intermediate temperatures | en_HK |
dc.type | Article | en_HK |
dc.identifier.openurl | http://library.hku.hk:4550/resserv?sid=HKU:IR&issn=0378-7753&volume=185&spage=233&epage=240&date=2008&atitle=An+improved+electrochemical+model+for+the+NH3+fed+proton+conducting+solid+oxide+fuel+cells+at+intermediate+temperatures | 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.jpowsour.2008.07.023 | en_HK |
dc.identifier.scopus | eid_2-s2.0-50949132837 | en_HK |
dc.identifier.hkuros | 153390 | en_HK |
dc.relation.references | http://www.scopus.com/mlt/select.url?eid=2-s2.0-50949132837&selection=ref&src=s&origin=recordpage | en_HK |
dc.identifier.volume | 185 | en_HK |
dc.identifier.issue | 1 | en_HK |
dc.identifier.spage | 233 | en_HK |
dc.identifier.epage | 240 | en_HK |
dc.identifier.isi | WOS:000259906600036 | - |
dc.publisher.place | Switzerland | 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 | 0378-7753 | - |