Abstract

The synthesis of high specific surface area molybdenum oxycarbide hydrocarbon isomerization catalysts has been achieved from low surface area molybdenum oxide or high surface area molybdenum carbide. A comparison of the molybdenum oxycarbide catalysts, prepared from both sources, with two classical platinum isomerization catalysts, supported on γ-alumina and on β-zeolite, for the isomerization of n-hexane, n-heptane and n-octane is presented, both at atmospheric pressure and elevated pressure. It is demonstrated that a high selectivity to the isomer products can be obtained for the reaction of n-heptane and n-octane even at very high conversion over the molybdenum catalysts. This is not possible over the platinum catalysts at high conversion due to extensive cracking of the C6+ alkanes and is due to differences in the isomerization mechanism. Further, these molybdenum based catalysts are highly active. Evidence is also presented for the non-bifunctional mechanism operating over the molybdenum oxycarbides: the metallacyclobutane bond shift mechanism.

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