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DC Field | Value | Language |
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dc.contributor.author | Chatrattanawet N. | |
dc.contributor.author | Saebea D. | |
dc.contributor.author | Authayanun S. | |
dc.contributor.author | Arpornwichanop A. | |
dc.contributor.author | Patcharavorachot Y. | |
dc.date.accessioned | 2021-04-05T03:21:37Z | - |
dc.date.available | 2021-04-05T03:21:37Z | - |
dc.date.issued | 2018 | |
dc.identifier.issn | 3605442 | |
dc.identifier.other | 2-s2.0-85021350626 | |
dc.identifier.uri | https://ir.swu.ac.th/jspui/handle/123456789/12794 | - |
dc.identifier.uri | https://www.scopus.com/inward/record.uri?eid=2-s2.0-85021350626&doi=10.1016%2fj.energy.2017.06.125&partnerID=40&md5=1c537c9be4eaf3711457de24b13980b1 | |
dc.description.abstract | In this work, solid oxide fuel cells (SOFCs) using biogas as the fuel with two different reforming approaches, i.e., external and internal reforming, were studied to determine the optimal operation conditions for each approach. Thermodynamic analysis was performed using a flowsheet simulator. The equilibrium gas composition was calculated by minimizing the Gibbs free energy. An electrochemical model that includes three voltage losses (i.e., activation, ohmic, and concentration losses) was used to predict the performance of the SOFCs. The simulation results showed that the reformer in the external reforming SOFC should be operated at a temperature of 973 K, a pressure of 1 atm, and a steam-to-carbon molar ratio of 0.5. In performance analysis, the simulation results indicated that both approaches have the same optimal operating conditions, i.e. a temperature of 1173 K, a pressure of 3 atm, and a current density of 5000 A/m2. Under the same operating conditions, the internal reforming SOFC exhibited better electrical efficiency than that of the external reforming SOFC. Considering the CO2 and CO emissions, the exhaust gas obtained from the anode side of the internal reforming SOFC contained 7.4% CO2 and 37.9% CO, which are higher values than those for the external reforming SOFC (1.9% CO2 and 32.5% CO). © 2017 Elsevier Ltd | |
dc.subject | Biogas | |
dc.subject | Carbon | |
dc.subject | Carbon dioxide | |
dc.subject | Exhaust gases | |
dc.subject | Fuel cells | |
dc.subject | Gas emissions | |
dc.subject | Reforming reactions | |
dc.subject | Steam reforming | |
dc.subject | Thermoanalysis | |
dc.subject | Thermodynamic properties | |
dc.subject | Electrical efficiency | |
dc.subject | Electrochemical modeling | |
dc.subject | Environmental studies | |
dc.subject | Internal reforming sofc | |
dc.subject | Optimal operating conditions | |
dc.subject | Optimal operation conditions | |
dc.subject | Solid oxide fuel cells (SOFCs) | |
dc.subject | Thermo dynamic analysis | |
dc.subject | Solid oxide fuel cells (SOFC) | |
dc.subject | biogas | |
dc.subject | electrochemical method | |
dc.subject | energy efficiency | |
dc.subject | fuel cell | |
dc.subject | Gibbs free energy | |
dc.subject | operations technology | |
dc.subject | performance assessment | |
dc.subject | solid | |
dc.subject | thermodynamics | |
dc.title | Performance and environmental study of a biogas-fuelled solid oxide fuel cell with different reforming approaches | |
dc.type | Article | |
dc.rights.holder | Scopus | |
dc.identifier.bibliograpycitation | Energy. Vol 146, (2018), p.131-140 | |
dc.identifier.doi | 10.1016/j.energy.2017.06.125 | |
Appears in Collections: | Scopus 1983-2021 |
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