The catalytic behaviour of the molybdenum oxycarbide catalyst, synthes
ized in situ from molybdenum oxide, is compared with that of a support
ed bifunctional platinum catalyst for the isomerization of n-octane. T
he main products are the mono- and di-methyl isomers, and almost no ar
omatics are observed. It is shown that a high selectivity to the isome
r products(> 90%) can be obtained over the molybdenum catalyst, even c
lose to the thermodynamic equilibrium (i.e., at high conversion (75%))
, while this is not possible over the platinum catalyst. Furthermore,
the high resistance of the molybdenum catalyst to sulphur and nitrogen
catalyst poisons typically found in crude oil is shown, and the isome
rization of n-heptane over a supported molybdenum oxycarbide (MoO3/SiC
) catalyst is demonstrated.