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    • 7. 发明授权
    • Increasing the level of 2-methyl-2-butene in isoamylene
    • 提高了亚甲基2-甲基-2-丁烯的含量
    • US5073663A
    • 1991-12-17
    • US472844
    • 1990-01-31
    • Gustavo CerriRobert C. Michaelson
    • Gustavo CerriRobert C. Michaelson
    • B01J31/08B01J21/16C07B61/00C07C5/25C07C7/04C07C7/148C07C11/10
    • C07C7/14875Y10S203/20
    • A method for increasing the ratio of 2-methyl-2-butene (2MB2) to 2-methyl-1-butene (2MB1) in isoamylenes involves fractionating a feedstream containing tertiary amyl methyl ether (TAME) and isoamylenes including 2MB2 and 2MB1 in a ratio of about 2:1 to effect a separation between an overhead hydrocarbon fraction of isoamylenes including 2MB2 and 2MB1 in a ratio of about 1:1, a bottoms fraction including TAME, and a sidestream hydrocarbon fraction consisting essentially of isoamylenes including 2MB2 and 2MB1 in a ratio of about 6 to 12:1, recovering the sidestream hydrocarbon fraction, and recycling the overhead hydrocarbon fraction of isoamylenes to form a mixture which is subsequently reacted to form the feedstream. Prior to fractionation, the feedstream is formed by passing isoamylene, and optionally TAME, in a vapor phase over an ether cracking catalyst which isomerizes isoamylene and converts 2MB1 to 2MB2, i.e., the feedstream for fractionating, which contains 2MB2 and 2MB1 in a ratio of 2 to 5:1. A method for converting 2-methyl-1-butene to 2-methyl-2-butene which may be used to form the feedstream for fractionating involves providing a hydrocarbon stream comprising isoamylenes including 2MB1 and 2MB2 in a ratio of within the range of 1:1 to 5, adding about TAME to the isoamylenes to form a mixture which is passed in the liquid phase at a temperature and a LHSV which favors isomerization over an acidic ion exchange resin catalyst to produce a reaction product including 2MB1, 2MB2 in a ratio of 1:6 to 12, and TAME.
    • 在异戊烯中增加2-甲基-2-丁烯(2MB2)与2-甲基-1-丁烯(2MB1)的比例的方法包括在含有叔戊基甲基醚(TAME)和包含2MB2和2MB1的异戊烯的进料流中 比例为约2:1,以使比例约为1:1的异戊二烯的塔顶烃馏分与包含TAME的底部馏分和基本上由2MB2和2MB1组成的异戊烯组成的侧流烃馏分 约6至12:1的比例,回收侧流烃馏分,以及再循环异戊烯的塔顶烃馏分以形成随后反应形成进料流的混合物。 在分馏之前,通过使异戊烯和任选的TAME通过使异戊烯异构化的醚裂化催化剂将异戊烯和任选的TAME通过异丙烯和任选的TAME形成,并将2MB1转化为2MB2,即用于分馏的原料流,其含有2MB2和2MB1, 2到5:1。 可用于形成用于分馏的原料流的2-甲基-1-丁烯至2-甲基-2-丁烯的方法包括提供包含2MB1和2MB2的异戊烯的烃流,其比例范围为1: 1至5,向异戊烯加入约TAME以形成在温度下通过液相的混合物,并且在酸性离子交换树脂催化剂上有利于异构化的LHSV以产生包含2MB1,2MB2的反应产物,其比例为 1:6到12,和TAME。