2012
DOI: 10.1016/j.jpowsour.2011.12.029
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Selection of suitable operating conditions for planar anode-supported direct-internal-reforming solid-oxide fuel cell

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Cited by 48 publications
(34 citation statements)
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“…The values of C 1 and C 2 are given in Table 6, based on the data provided by Wongchanapai [47], for each of the fuel cell component. Values of L k for the different components, required for the calculation of ohmic losses, are listed in Table 7.…”
Section: Solid Oxide Fuel Cellmentioning
confidence: 99%
“…The values of C 1 and C 2 are given in Table 6, based on the data provided by Wongchanapai [47], for each of the fuel cell component. Values of L k for the different components, required for the calculation of ohmic losses, are listed in Table 7.…”
Section: Solid Oxide Fuel Cellmentioning
confidence: 99%
“…1. A 1D model of direct internal reforming planar SOFC, capable of internal reforming of the methane in the syngas into hydrogen, was developed in the previous work by the authors [14] and applied to this study. On the other hand, thermodynamic equilibrium model is used for biomass gasification.…”
Section: System Configuration and Descriptionmentioning
confidence: 99%
“…SOFC, Gasifier, HXs, burner, HRSG, air and fuel compressors, were thermodynamically modeled under steady-state operations. Mass and energy balances were applied for each component using lumped models, which consider each component as a control volume with the exception of a 1D SOFC model [14]. The assumptions made for developing the system model are given as: (i) all system components operate under steady-state conditions; (ii) all gas mixtures behave as ideal gases; (iii) heat losses from SOFC and gasifier to the environment are negligible and heat losses in HXs and the HRSG are assumed 2% of heat transferred; (iv) chemical reactions are assumed to be in equilibrium.…”
Section: System Modelingmentioning
confidence: 99%
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