Raising the Selectivity of the Unsteady-State Oxidative Dehydrogenation of n-Butane in a Two-Reactor System with a Circulating Catalyst

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A mathematical model of oxidative dehydrogenation of n-butane is proposed. It is based on a kinetic model and takes into consideration two types of catalytic center. Ways of raising the divinyl formation selectivity of the process in a two-reactor system with a circulating catalyst are found.

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