首页> 外国专利> The process and system of 1-hexeno production by buteno include distillation of butenos, catalytic met, isomerization, separation of hexenos, thermal integration between capacitance of fractionator and background current of distillation column, and a-oil fine separation process. '

The process and system of 1-hexeno production by buteno include distillation of butenos, catalytic met, isomerization, separation of hexenos, thermal integration between capacitance of fractionator and background current of distillation column, and a-oil fine separation process. '

机译:丁烯生产1-己烯的方法和系统包括丁烯的蒸馏,催化法,异构化,己烯的分离,分馏塔的容量与蒸馏塔的背景电流之间的热集成以及a油精分离过程。 ”

摘要

Processes and systems for producing linear alpha olefins are described herein. One embodiment is a process comprising: a) separating a mixed butene stream comprising 1 -butene and 2-butene into an overhead 1 -butene stream and a bottoms 2-butene stream in a butene distillation column, a portion of the bottoms 2-butene stream being separated to form a butene reboiler stream that is heated and vaporized in a reboiler and returned to the butene distillation column, (b) subjecting at least a portion of the overhead 1 -butene stream from (a) to catalytic metathesis to produce an effluent including 3-hexene, (c) isomerizing 3-hexene from (b) to produce a mixed hexene stream comprising 1 -hexene, 2-hexene and 3-hexene, (d) separating the mixed hexene stream in a hexene fractionation tower to form a 1 -hexene vapor overhead stream that is condensed in a cooler and a bottoms stream comprising 2-hexene and 3-hexene, and (e) using heat obtained by condensing the 1 -hexene vapor overhead stream of (d) to heat the butene reboiler stream of (a). Another embodiment is a superfractionation process. Corresponding systems are also disclosed.
机译:本文描述了生产线性α-烯烃的方法和系统。一个实施方案是一种方法,其包括:a)在丁烯蒸馏塔中将包含1-丁烯和2-丁烯的混合丁烯料流分离成塔顶1-丁烯料流和塔底物2-丁烯料流,塔底物2-丁烯的一部分。物流被分离以形成丁烯再沸器物流,该物流在再沸器中被加热和汽化并返回到丁烯蒸馏塔,(b)使来自(a)的至少一部分塔顶1-丁烯物流进行催化复分解以产生含3-己烯的废水,(c)将(b)中的3-己烯异构化以生成包含1-己烯,2-己烯和3-己烯的混合己烯物流,(d)在己烯分馏塔中将混合己烯物流分离为形成在冷却器中冷凝的1-己烯蒸气塔顶物流和包含2-己烯和3-己烯的塔底物流,以及(e)使用通过冷凝(d)的1-己烯蒸气塔顶物流加热得到的热量(a)的丁烯再沸器物流。另一个实施方案是超分馏方法。还公开了相应的系统。

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