2007
DOI: 10.1016/j.electacta.2007.08.046
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Analysis of a solid oxide fuel cell system for combined heat and power applications under non-nominal conditions

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Cited by 75 publications
(37 citation statements)
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“…Finally, It is assumed that methane cannot be electrochemically oxidized. This approach is in good accordance with the modeling done in a similar case by [10].…”
Section: Thermochemical Modelsupporting
confidence: 84%
“…Finally, It is assumed that methane cannot be electrochemically oxidized. This approach is in good accordance with the modeling done in a similar case by [10].…”
Section: Thermochemical Modelsupporting
confidence: 84%
“…, n in CO , n in CH 4 are molar flow rates of the hydrogen, carbon monoxide and methane entering the burner, while∆Ĥ H 2 ,∆Ĥ CO ,∆Ĥ CH 4 are the specific heats of reaction. C p,i is the specific heat of the reactants entering the burner, n in i and n out i are the molar flow rate of the reactants entering and exiting the burner.…”
Section: Burnermentioning
confidence: 99%
“…The methane was fed to the CPO x reformer for conversion to syngas consisting of H 2 , H 2 O, CO, CO 2 , O 2 and unreacted CH 4 . The hydrogen and carbon monoxide from the reformer were fed to the 1st stage SOFC stack to generate electric power and heat.…”
Section: Cpox Reformermentioning
confidence: 99%
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“…The generated electric power by current fuel cells ranges from 3 to 1000kW and can reach up to 10,000kW. Fuel cell technology is mainly used in applications of small and medium scale power systems [46,[48][49][50].…”
Section: Fuel Cellsmentioning
confidence: 99%