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PROCESS FOR THE RECOVERY OF 1,2-DICHLOROPROPANE FROM THE EXHAUST GASES RESULTING FROM PROPENE-OXIDE PREPARATION

机译:从环氧丙烷制备产生的排气中回收1,2-二氯丙烷的方法

摘要

The invention relates to a process for the advanced recovery of 1,2-di-chloro-propane from the exhaust gases resulting from propene oxide preparation, that is also applicable to the advanced removal of other chlorinated products from purged flows resulting from petrochemical processes. According to the invention, the process consists in that, during a first stage, the absorption of 1,2-di-chloro-propane from the exhaust gases in 2-ethyl-hexanol is achieved at a temperature of 40...50A C and a pressure of 1.5...7 bar, followed by the fractionation of the resulting mixture in a distillation column where a top fraction consisting of the mixture of 1,2-di-chloro-propane and inert gases is separated, said mixture being further condensed and cooled down to a temperature of 40A C and a pressure of 1.1...1.6 bar and passed into a reflux vessel wherefrom one part of the resulting 1,2-di-chloro-propane condensation product is sent to the top of the distillation column, while the other part is delivered as a final product, the uncondensed gaseous flow in the reflux vessel passing into an 1,2-di-chloro-propane adsorption system on active carbon, wherefrom, after the steam desorption of 1,2-di-chloro-propane, it is condensed and separated from water.
机译:本发明涉及一种用于从环氧丙烷制备所产生的废气中高级回收1,2-二氯丙烷的方法,该方法还适用于从石油化学方法所产生的吹扫流中高级去除其他氯化产物。根据本发明,该方法在于,在第一阶段中,在40 ... 50A C的温度下从2-乙基己醇中的废气中吸收1,2-二氯丙烷在1.5 ... 7 bar的压力下,随后将所得混合物在蒸馏塔中分馏,在该蒸馏塔中分离出由1,2-二氯丙烷和惰性气体的混合物组成的顶部馏分,所述混合物为进一步冷凝并冷却至40°C的温度和1.1 ... 1.6 bar的压力,并进入回流容器,然后将一部分所得的1,2-二氯丙烷缩合产物送至反应釜的顶部。蒸馏塔,而另一部分作为最终产品交付时,回流容器中的未冷凝气流进入活性炭上的1,2-二氯丙烷吸附系统,在蒸汽解吸1之后, 2-二氯丙烷,将其冷凝并与水分离。

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