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High-purity 1-butene recovery from mixed butene streams - by isobutene polymerisation to gasoline and fractionation

机译:从混合丁烯流中回收高纯度的1-丁烯-通过异丁烯聚合成汽油并分馏

摘要

Recovery of 1-butene from C4 olefinic feeds is effected by (a) subjecting the feed to selective polymerisation to convert isobutene to gasoline; (b) fractionating the effluent from (a) to separate the gasoline from a fraction (I) comprising isobutane, n-butane, 1-butene, 2-butenes and a small amt. of isobutene; (c) deisobutanising (I); and (d) fractionating the deisobutanised stream to recover a fraction comprising mainly 2-butenes and n-butane and a fraction comprising at least 99 wt.% 1-butene. The process can be applied to C4 streams from catalytic or steam cracking units, giving high-purity 1-butene suitable for use as a comonomer in the mfr. of high-density polyethylene.
机译:通过(a)使进料进行选择性聚合以将异丁烯转化为汽油来实现从C 4烯烃进料中回收1-丁烯。 (b)将来自(a)的流出物分馏,以将汽油与包含异丁烷,正丁烷,1-丁烯,2-丁烯和少量氨的馏分(I)分离。异丁烯(c)去异丁烷化(I); (d)分馏去异丁烷料流以回收主要包含2-丁烯和正丁烷的馏分和包含至少99重量%的1-丁烯的馏分。该方法可以应用于来自催化裂化或蒸汽裂化装置的C4物流,得到适合用作mfr中共聚单体的高纯度1-丁烯。高密度聚乙烯。

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