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DC Field | Value | Language |
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dc.contributor.author | Namwong L. | |
dc.contributor.author | Authayanun S. | |
dc.contributor.author | Saebea D. | |
dc.contributor.author | Patcharavorachot Y. | |
dc.contributor.author | Arpornwichanop A. | |
dc.date.accessioned | 2021-04-05T03:23:24Z | - |
dc.date.available | 2021-04-05T03:23:24Z | - |
dc.date.issued | 2016 | |
dc.identifier.issn | 3787753 | |
dc.identifier.other | 2-s2.0-84988468494 | |
dc.identifier.uri | https://ir.swu.ac.th/jspui/handle/123456789/13347 | - |
dc.identifier.uri | https://www.scopus.com/inward/record.uri?eid=2-s2.0-84988468494&doi=10.1016%2fj.jpowsour.2016.09.042&partnerID=40&md5=94b40249f217a9726596a3086ea8de56 | |
dc.description.abstract | Proton-conducting solid oxide electrolysis cells (SOEC-H+) are a promising technology that can utilize carbon dioxide to produce syngas. In this work, a detailed electrochemical model was developed to predict the behavior of SOEC-H+ and to prove the assumption that the syngas is produced through a reversible water gas-shift (RWGS) reaction. The simulation results obtained from the model, which took into account all of the cell voltage losses (i.e., ohmic, activation, and concentration losses), were validated using experimental data to evaluate the unknown parameters. The developed model was employed to examine the structural and operational parameters. It is found that the cathode-supported SOEC-H+ is the best configuration because it requires the lowest cell potential. SOEC-H+ operated favorably at high temperatures and low pressures. Furthermore, the simulation results revealed that the optimal S/C molar ratio for syngas production, which can be used for methanol synthesis, is approximately 3.9 (at a constant temperature and pressure). The SOEC-H+ was optimized using a response surface methodology, which was used to determine the optimal operating conditions to minimize the cell potential and maximize the carbon dioxide flow rate. © 2016 Elsevier B.V. | |
dc.subject | Carbon dioxide | |
dc.subject | Cells | |
dc.subject | Cytology | |
dc.subject | Electrolysis | |
dc.subject | Electrolytic cells | |
dc.subject | Optimization | |
dc.subject | Regenerative fuel cells | |
dc.subject | Synthesis gas | |
dc.subject | Synthesis gas manufacture | |
dc.subject | Water gas shift | |
dc.subject | Electrochemical modeling | |
dc.subject | Electrolysis cell | |
dc.subject | Modeling and optimization | |
dc.subject | Operational parameters | |
dc.subject | Optimal operating conditions | |
dc.subject | Proton conducting solids | |
dc.subject | Response surface methodology | |
dc.subject | Syn-gas | |
dc.subject | Solid oxide fuel cells (SOFC) | |
dc.title | Modeling and optimization of proton-conducting solid oxide electrolysis cell: Conversion of CO2 into value-added products | |
dc.type | Article | |
dc.rights.holder | Scopus | |
dc.identifier.bibliograpycitation | Journal of Power Sources. Vol 331, (2016), p.515-526 | |
dc.identifier.doi | 10.1016/j.jpowsour.2016.09.042 | |
Appears in Collections: | Scopus 1983-2021 |
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