Kinetics of the hydroisomerization of n-hexane on nickel containing zeolites
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Development of adequate models describing the kinetics of hydroisomerization and hydrocracking of n-hexane over bifunctional zeolite catalysts. The dehydrogenation is assumed to be the rate limiting step and not the isomerization. With the derived model the reaction at presence of inert gas can be described better than with Froment's model and without inert gas with similar accuracy