Abstract
The flue gas which resulted from oxidation of the fuel flow in the SOFC stack was burnt off in the catalytic combustor under the operating condition acquired by the process simulation. Conversion of the combustible components in the stack flue gas was experimentally measured at four different GHSVs in a tubular reactor packed with base-metal catalyst pellets. Optimum GHSV of 6,990 hr-1 in the catalytic combustor was determined on the basis of reactor performance including pressure drop, carbon monoxide slip, and conversion of the combustible components.
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