MODELING OF n-BUTANE OXIDATIVE DEHYDROGENATION IN A DUAL-REACTOR SYSTEM


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Abstract

Mathematical modeling of the oxidative dehydrogenation of n-butane into butadiene in a dual-reactor system with separate reactants feeding has been performed. The factors affecting the butadiene selectivity enhancement have been studied. It has been shown that it is possible to regulate the state of a catalyst in the reaction zone by varying the rate of catalyst circulation between the reactors.

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