The bimetallic carbide catalyst Co₆W₆C, which has been used to advantage in the dry reforming of methane, is considered here for the steam reforming of methanol. Such a process would be an effective way to produce hydrogen on demand and on location using a liquid fuel. Preliminary data indicate that acceptable values of the methanol/water ratio are bounded by low activity (excess water) and rapid plugging (excess methanol). A value of 1.5 (weight basis) appears appropriate. Simple kinetics indicates that a pseudo-second-order reaction rate constant for this reaction is at least comparable to that obtained for the dry reforming reaction.

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