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method for separating isoprene by two-stage extraktiver distillation

机译:两级萃取剂蒸馏分离异戊二烯的方法

摘要

Isoprene is recovered in high purity from a cyclopentadiene-containing C5 fraction in a two-stage extractive distillation in the presence of a selective polar solvent. Substantially all of the cyclopentadiene is removed in the first or heavy ends extractive distillation zone wherein the concentration of the extractive distillation solvent is maintained at from 5 to 40 mole percent to thereby recover substantially all of the isoprene and more volatile hydrocarbons as overhead products from the zone. Isoprene is then separated from this overhead C5 fraction in a second or light ends extractive distillation zone and is recovered in the fat solvent from which it is recovered in an isoprene stripping zone. A high solvent concentration is maintained in the upper section of the isoprene stripping zone and cyclopentadiene is recovered from a lower section of the zone via a side draw. The dimer content of the solvent circulating in the light ends extractive distillation zone and isoprene stripping zone is controlled by recycling a portion of the stripped solvent from the bottom of the isoprene stripping zone to the heavy ends extractive distillation zone wherein the recovered dimer is rejected in the bottoms product. Solvent is recovered from that bottoms product in a heavy ends stripping zone as a vapor side draw.
机译:在选择性极性溶剂的存在下,在两步萃取蒸馏中,从含环戊二烯的C5馏分中以高纯度回收异戊二烯。基本上所有的环戊二烯在第一或重馏分萃取蒸馏区中被除去,其中萃取蒸馏溶剂的浓度保持在5至40摩尔%,从而从塔顶馏出物中回收塔顶产物中基本上所有的异戊二烯和更具挥发性的烃。区。然后在第二或轻馏分萃取蒸馏区中从该塔顶馏出的C5馏分中分离出异戊二烯,并在脂肪溶剂中进行回收,然后在异戊二烯汽提区中从中回收异戊二烯。在异戊二烯汽提区的上部保持高溶剂浓度,并且通过侧馏分从该区的下部回收环戊二烯。在轻馏分萃取蒸馏区和异戊二烯汽提区中循环的溶剂的二聚体含量是通过将一部分汽提的溶剂从异戊二烯汽提区的底部再循环到重馏分萃取蒸馏区来控制的,在重馏分萃取蒸馏区中回收的二聚体被拒绝。底部产品。在重质馏分汽提区从塔底产物中回收溶剂,作为蒸汽侧馏分。

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