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Process for the production and purification of N-Butyl acrylate.

机译:丙烯酸正丁酯的生产和纯化方法。

摘要

A process for the production of n-butyl acrylate (BuAcA) including the steps of esterifying acrylic acid (HAcA) with a n-butanol (n-BuOH) in a reaction zone, obtaining a condensate from the overhead vapors from the reaction zone which separates into organic and aqueous phases, feeding the organic phase comprising a major portion of BuAcA and minor portions of BuOH, water and light ends impurities to a finishing fractionation zone from which is obtained a side stream of a finished high purity BuAcA and an overhead condensate comprising BuAcA, BuOH, water, and light ends, recycling most of the overhead condensate from the finishing zone to the reaction zone, feeding the remainder of such condensate to a purge recovery zone together with a stream of makeup water, obtaining an overhead condensate from the purge recovery zone which separates into organic and aqueous phases each containing a portion of light ends produced in the reaction, recycling a portion of the organic phase as reflux to the purge recovery zone and discarding the remainder, and recycling at least a portion of the aqueous phase as feed to the purge recovery zone and discarding any remainder. Discarding of portions of the two phases of the overhead condensate has the effect of preventing or retarding the buildup of light ends in the system, while the amounts of water in the water makeup stream and the recycled portion of the aqueous phase of the overhead condensate to the purge recovery zone forms low-boiling azeotropes with components of the light ends thus facilitating separation of the light ends from the BuAcA and BuOH in the purged portion of the finishing zone overhead.
机译:一种生产丙烯酸正丁酯(BuAcA)的方法,包括以下步骤:在反应区中用正丁醇(n-BuOH)将丙烯酸(HAcA)酯化,从反应区的塔顶蒸气中获得冷凝液,分离成有机相和水相,将包含大部分BuAcA和少量BuOH,水和轻馏分杂质的有机相进料到精馏分馏区,从中获得精制高纯度BuAcA和塔顶冷凝液的支流包括BuAcA,BuOH,水和轻馏分,将大部分塔顶冷凝物从精制区循环到反应区,将剩余的此类冷凝物与补充水流一起送入吹扫回收区,从中获得塔顶冷凝物。吹扫回收区,分为有机相和水相,每个有机相包含反应中产生的一部分轻质馏分,将一部分有机相作为回流物再循环至吹扫回收区并丢弃剩余物,并将至少一部分水相作为原料循环到吹扫回收区并丢弃任何剩余物。丢弃塔顶冷凝物两相的一部分具有防止或延迟系统中轻馏分积聚的作用,而补给水和塔顶冷凝物水相的再循环部分中的水量可以减少或减少。吹扫恢复区与轻馏分的组分形成低沸点共沸物,从而促进轻馏分与精馏区塔顶吹扫部分中的BuAcA和BuOH分离。

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