首页> 外国专利> PREPARATION OF PROPILANIUM BY MEANS OF SIMULTANEOUS DEHYDRATATION AND SKELETAL ISOMERIZATION OF ISOBUTANOL ON ACID CATALYSTS WITH A FOLLOWING METATHESIS

PREPARATION OF PROPILANIUM BY MEANS OF SIMULTANEOUS DEHYDRATATION AND SKELETAL ISOMERIZATION OF ISOBUTANOL ON ACID CATALYSTS WITH A FOLLOWING METATHESIS

机译:异丁香酸催化剂上同时脱水和异丁醇骨架异构化制备PI的研究。

摘要

The present invention relates to a method for producing propylene, in which at the first stage isobutanol is subjected to simultaneous dehydration and skeletal isomerization to obtain mainly the corresponding olefins having the same number of carbon atoms and essentially including a mixture of n-butenes and isobutene, and the second stage, n-butenes are subjected to metathesis, the method includes the steps of: a) introducing into the reactor a stream (A) including isobutanol, optionally water, an optionally inert component, b) said stream bring into contact with the catalyst in the specified reactor under conditions effective for the dehydration and skeletal isomerization of at least part of isobutanol to obtain a mixture of n-butenes and isobutene, c) the stream (B) is captured from the said reactor, water, the inert component, are removed if it is present, and unreacted isobutanol, if present, to obtain a mixture of n-butenes and isobutene, d) fractionate the mixture to obtain a stream of n-butenes (N) and to remove the main part of isobutene, optionally recycled from outflow (A), to the dehydration / isomerization reactor from step b), e) the stream (N) is directed to the metathesis reactor and the stream (N) is contacted with the catalyst in the specified metathesis reactor, optionally in the presence of ethylene, under conditions effective to produce propylene, f) capture stream (P) from said metathesis reactor, comprising mainly propylene, unreacted n-butenes, heavy fractions, optionally unreacted ethylene, g) fractionate stream (P) to trap propylene, and optional recycle unreacted
机译:本发明涉及一种生产丙烯的方法,其中在第一步中,异丁醇同时进行脱水和骨架异构化,主要得到相应的具有相同碳原子数并且基本上包括正丁烯和异丁烯的混合物的烯烃。第二步,对正丁烯进行复分解,该方法包括以下步骤:a)将包含异丁醇,任选地水,任选地惰性组分的料流(A)引入反应器中,b)使所述料流接触在特定反应器中使用催化剂在至少一部分异丁醇脱水和骨架异构化的有效条件下获得正丁烯和异丁烯的混合物,c)从所述反应器,水,除去惰性组分(如果存在),然后除去未反应的异丁醇(如果存在),以获得正丁烯和异丁烯的混合物,d)分馏该混合物以获得一种将正丁烯(N)馏分并从步骤(b)的脱水/异构化反应器中除去异丁烯的主要部分(视需要从流出液(A)中再循环),将e)料流(N)导入复分解反应器中,物流(N)在指定的复分解反应器中,任选在乙烯的存在下,在有效产生丙烯的条件下与催化剂接触,f)从所述复分解反应器中捕获主要包含丙烯,未反应的正丁烯的物流(P)。 ,重馏分,可选地未反应的乙烯,g)分馏物流(P)以捕集丙烯,以及可选地未反应的再循环

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