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Process for the preparation of ethyl tert-butyl ether from C4-hydrocarbon cuts

机译:由C4-烃馏分制备乙基叔丁基醚的方法

摘要

Production of ethyl tertiary butylether (ETBE) from 4C-hydrocarbons mixture (I), comprises: (a) reaction of parts of the isobutene with ethanol in the presence of an acid catalyst to ETBE; (b) separation of the non-converted 4C-hydrocarbons (III) under receipt of a fraction (II) exhibiting ETBE; (c) distillative separation of the 4C-hydrocarbons (III) into a fraction (IV) and an isobutene-free fraction (V) containing at least 2-butene and n-butane; and (d) renewed reaction of the isobutene in fraction (IV) with ethanol (VI) to ETBE and separating non-converted 4C-hydrocarbon. Production of ethyl tertiary butylether (ETBE) from technical mixtures of 4C-hydrocarbons (I), which contain at least 1-butene, isobutene, n-butane and 2-butene, comprises: (a) reaction of parts of the isobutene with ethanol in the presence of an acid catalyst to ETBE; (b) separation of the non-converted 4C-hydrocarbons (III) from the discharge of the step (a) by thermal separation processes under receipt of a fraction (II) exhibiting ETBE; (c) distillative separation of the 4C-hydrocarbons (III) into a fraction (IV) containing at least 1-butene and isobutene and an almost isobutene-free fraction (V) containing at least 2-butene and n-butane; (d) renewed reaction of the isobutene contained in fraction (IV) with ethanol (VI) in the presence of an acid catalyst to ETBE; and (e) separation of the non-converted 4C-hydrocarbons (VIII) from the discharge of step (d) under receipt of a fraction (VII) exhibiting ETBE. An independent claim is included for a composition comprising larger than 90 mass proportions of ETBE, 0-5 mass proportions of ethanol, 0-2.5 mass proportions of tertiary butanol, =1.5 mass proportions of hydrocarbons with 5 or more carbon atoms and =1 mass proportion of 4C-hydrocarbons.
机译:由4C-烃混合物(I)生产乙基叔丁基醚(ETBE)包括:(a)使异丁烯的一部分与乙醇在酸催化剂的存在下反应成ETBE; (b)在接收到具有ETBE的馏分(II)的情况下分离未转化的4C-烃(III); (c)将4C-烃(III)蒸馏分离成馏分(IV)和含有至少2-丁烯和正丁烷的不含异丁烯的馏分(V); (d)将馏分(IV)中的异丁烯与乙醇(VI)重新反应为ETBE,并分离未转化的4C-烃。由至少包含1-丁烯,异丁烯,正丁烷和2-丁烯的4C烃的工业混合物(I)生产乙基叔丁醚(ETBE)包括:(a)部分异丁烯与乙醇反应在ETBE的酸催化剂存在下; (b)在接收到具有ETBE的馏分(II)的情况下,通过热分离方法从步骤(a)的排出物中分离出未转化的4C烃(III); (c)将4C烃(III)蒸馏分离成至少含有1-丁烯和异丁烯的馏分(IV)和至少含有2-丁烯和正丁烷的几乎不含异丁烯的馏分(V); (d)在酸催化剂的存在下,将馏分(IV)中包含的异丁烯与乙醇(VI)重新反应为ETBE; (e)在接收到具有ETBE的馏分(VII)的情况下,从步骤(d)的排放中分离出未转化的4C烃(VIII)。对于包含大于90质量份的ETBE,0-5质量份的乙醇,0-2.5质量份的叔丁醇,= 1.5质量份的具有5个以上碳原子的烃和= 1质量份的组合物,包括一个独立的权利要求4C烃的比例。

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