Abstract

Abstract Oxidative dehydrogenation of n- butene isomers to 1,3-butadiene was carried out over a multicomponent bismuth molybdate (Co 9 Fe 3 Bi 1 Mo 12 O 51 ) catalyst. The yield for 1,3-butadiene over the catalyst decreased in the order of 1-butene > mixture of 1-butene and 2-butene > 2-butene. The oxidative dehydrogenation of n- butene to 1,3-butadiene favorably occurred with increasing 1-butene content, while the total oxidation of n- butene to CO 2 was promoted with increasing 2-butene content. It is believed that the Co 9 Fe 3 Bi 1 Mo 12 O 51 catalyst retained more selective oxygen species for the reaction with 1-butene than for the reaction with 2-butene, leading to the facile oxidative dehydrogenation of 1-butene to 1,3-butadiene.

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