Please use this identifier to cite or link to this item: https://ir.swu.ac.th/jspui/handle/123456789/12004
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dc.contributor.authorSaebea D.
dc.contributor.authorAuthayanun S.
dc.contributor.authorPatcharavorachot Y.
dc.date.accessioned2021-04-05T03:01:36Z-
dc.date.available2021-04-05T03:01:36Z-
dc.date.issued2020
dc.identifier.issn23524847
dc.identifier.other2-s2.0-85081096162
dc.identifier.urihttps://ir.swu.ac.th/jspui/handle/123456789/12004-
dc.identifier.urihttps://www.scopus.com/inward/record.uri?eid=2-s2.0-85081096162&doi=10.1016%2fj.egyr.2019.08.078&partnerID=40&md5=5f6a1603fb08239e711159955a994c5b
dc.description.abstractThis work aims to study on the performance of the SDC-based SOFC with a direct internal reforming of methane at lower temperature in the range of 600–750 ºC. The model of SDC-based SOFC with direct internal reforming mode is simulated and validated. The predicted results are in a good agreement with experimental data. The simulated results indicate that the molar flow rate of the hydrogen produced from the methane steam reforming reaction is higher as an increasing temperature. Moreover, the cathode activation overpotential is obviously reduced. Thus, the increase of temperature from 600 to 700 °C can enhance the average power density of SOFC from 0.19 to 0.42 A/m2. © 2019
dc.subjectElectrolytes
dc.subjectMethane
dc.subjectSolid oxide fuel cells (SOFC)
dc.subjectTemperature
dc.subjectCathode activation
dc.subjectDirect internal reforming
dc.subjectIncreasing temperatures
dc.subjectLow temperatures
dc.subjectLower temperatures
dc.subjectPerformance analysis
dc.subjectSimulated results
dc.subjectSteam reforming of methane
dc.subjectSteam reforming
dc.titlePerformance analysis of direct steam reforming of methane in SOFC with SDC-based electrolyte
dc.typeConference Paper
dc.rights.holderScopus
dc.identifier.bibliograpycitationEnergy Reports. Vol 6, (2020), p.391-396
dc.identifier.doi10.1016/j.egyr.2019.08.078
Appears in Collections:Scopus 1983-2021

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