Abstract
Performance of the SOFC single cell with the CO 2 reforming catalyst was investigated utilizing CH 4 /CO 2 . It was found that the voltage in CH 4 /CO 2 was comparatively high against conventional steam reforming conditions even in high fuel utilization ranges. The process simulation was conducted to the model of 1 kW CO 2 reforming SOFC system with anode off gas recycling. The simulation results such as heat balance and recycling procedure suggested that the CO 2 reforming could be one of the feasible approach for high electrical efficiency SOFC system.
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CITATION STYLE
Kushi, T., Sato, H., Fujita, K., & Amaha, S. (2015). Feasibility of CO 2 Reforming SOFC System. ECS Transactions, 65(1), 25–31. https://doi.org/10.1149/06501.0025ecst
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