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Method for producing 1,3-butadiene from n- butene using a continuous-flow dual-bed reactor

机译:使用连续流双床反应器由正丁烯生产1,3-丁二烯的方法

摘要

Two catalysts is packed in a fixed bed reactor, using a continuous-flow dual-bed reactor designed catalyst layer 2 so as not mixed physically present invention, the oxidative dehydration of n- butene relates to a process for producing 1,3-butadiene by hydrogenation reaction. In particular, the present invention provides a multi-component molybdenum activity is different for the oxidative dehydrogenation reactions (1-butene, trans-2-butene, cis-2-butene) isomers of butene further n- By using a continuous-flow dual-bed reactor using a ferrite-based catalysts and bismuth based catalyst, as a reactant C4 mixture contained the n- butanes n- butene oxidative dehydrogenation of n- butene to a method capable of producing 1,3-butadiene by the reaction.
机译:将两种催化剂装填在固定床反应器中,使用连续流双床反应器设计的催化剂层2,以便不物理混合本发明,正丁烯的氧化脱水涉及一种通过以下方法生产1,3-丁二烯的方法氢化反应。特别地,本发明提供了对于丁烯的进一步n-的氧化脱氢反应(1-丁烯,反式-2-丁烯,顺式-2-丁烯)异构体的多组分钼活性是不同的。床反应器使用铁氧体基催化剂和铋基催化剂,作为反应物C4混合物,包含正丁烷,正丁烯氧化正丁烯氧化脱氢的方法,该方法能够通过该反应生产1,3-丁二烯。

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