首页> 外国专利> METHOD FOR OBTAINING A CONJUGATED DIOLEFIN AND / OR OLEFIN FROM A C (DOWN ARROW) 4 (DOWN ARROW) - OR C (DOWN ARROW) 5 (DOWN ARROW) HYDROCARBON MIXTURE

METHOD FOR OBTAINING A CONJUGATED DIOLEFIN AND / OR OLEFIN FROM A C (DOWN ARROW) 4 (DOWN ARROW) - OR C (DOWN ARROW) 5 (DOWN ARROW) HYDROCARBON MIXTURE

机译:从C(向下箭头)4(向下箭头)-或C(向下箭头)5(向下箭头)烃混合物中获得共轭二烯烃和/或烯烃的方法

摘要

1. A process for recovering a conjugated diolefin and/or olefin or olefin mixture from a C4 - or C5 -hydrocarbon mixture which contains the conjugated diolefin and/or the olefin or olefins, hydrocarbons which are more sparingly soluble in the selective solvent than the said diolefin and/or the olefin or olefins, and hydrocarbons which are more readily soluble in the said solvent than the said diolefin and/or the olefin or olefins, the C4 - or C5 -hydrocarbon mixture being separated, by means of extractive distillation, into a distillate containing the more sparingly soluble hydrocarbons, a product stream containing the conjugated diolefin and/or the olefin or olefin mixture, and a stream containing the more readily soluble hydrocarbons, wherein the extractive distillation is carried out using - a distillate take-off zone (separation zone C), - a feed zone for the starting C4 - or C5 -hydrocarbon mixture (separation zone A), - a product take-off zone for the product stream (separation zone B) and - a stripping zone in which the selective solvent is recovered and from which the stream containing the more readily soluble hydrocarbons is taken off (separation zone D), and (a) the starting C4 - or C5 -hydrocarbon mixture is fed to separation zone A, (b) the selective solvent to be fed to the extractive distillation is introduced into the upper part of separation zone C, (c) some of the laden selective solvent obtained in the lower part of separation zone C is fed to the upper part of separation zone A and the remainder is fed to the upper part of separation zone B, (d) the laden selective solvent obtained in the lower part of separation zone A, and that obtained in the lower part of separation zone B, are fed to separation zone D, from which the stream containing the more readily soluble hydrocarbons, and a stream of the selective solvent which has been partially or completely freed from the hydrocarbons, are removed, (e) a product stream containing the conjugated diolefin and/or the olefin or olefin mixture is taken off from separation zone B, and (f) the distillate is removed from separation zone C.
机译:1.一种从包含共轭二烯烃和/或烯烃或烯烃的C 4-或C 5-烃混合物中回收共轭二烯烃和/或烯烃或烯烃混合物的方法,该烃比选择性溶剂更难溶于选择性溶剂。所述二烯烃和/或一种或多种烯烃,和比所述二烯烃和/或一种或多种烯烃更易溶于所述溶剂的烃,其中C 4-或C 5-烃混合物通过萃取蒸馏分离,进入含有较难溶的烃的馏出物,含有共轭二烯烃和/或烯烃或烯烃混合物的产物流和含有较易溶的烃的流,其中萃取蒸馏是使用-馏出物进行的区域(分离区C),-起始C4-或C5-碳氢化合物混合物的进料区(分离区A),-产物流的产物取出区(分离z B)和-汽提区,在其中回收选择性溶剂,并从其中除去含有较易溶的烃的物流(分离区D),和(a)进料起始的C4-或C5-烃混合物到分离区A,(b)将要进料到萃取蒸馏中的选择溶剂引入分离区C的上部,(c)将在分离区C的下部得到的一些负载的选择溶剂进料到分离区C。将分离区A的上部和其余部分进料到分离区B的上部,(d)在分离区A的下部获得的,在分离区B的下部获得的负载的选择性溶剂,将其送入分离区D,从中分离出含有较易溶的烃的料流,并除去已部分或完全从烃中分离出来的选择性溶剂的料流,(e)含有共轭二醇的产物料流从分离区B中除去烯烃和/或烯烃混合物中的烯烃和/或烯烃混合物,并且(f)从分离区C中除去馏出物。

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