Model propane oxidative dehydrogenation

The TPD/XPS results indicated that CO, propane and propene bind stronger to a reduced V-terminated 203(000 ) surface than to an oxidized V = 0 terminated surface. Nevertheless, vanadyl groups are probably required in the course of catalytic reactions. However, rates of propane oxidative dehydrogenation (ODH) to propene at atmospheric pressure are rather low and no reaction products were observed by gas chromatography, both for oxidized and reduced V Oj model surfaces at temperatures up to 500 K [12]. 

Over the years the range of uses of the K-L model has been extended to chemical processes that can not be described by first order kinetics. For these problems no anal3dical solution can be obtained so the resulting set of DAE equations are solved numerically. Gascon et al [48], for example, investigated the behavior of a two zone fluidized bed reactor for the propane dehydrogenation and n-butane partial oxidation processes emplo3ung the K-L model framework. 

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