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PURIFICATION OF ACETONITRILE BY DISTILLING RECOVERY BY DISTILLATION AND ION EXCHANGE RESIN TREATMENT PROCESS

机译:蒸馏提纯回收和离子交换树脂处理工艺提纯乙腈

摘要

PROBLEM TO BE SOLVED: To obtain a highly purified acetonitrile applicable to chromatography in a few process and a low cost by subjecting crude acetonitrile as a by-product in producing acrylonitrile to distillation and an ion exchange resin treatment. ;SOLUTION: The objective compound is obtained by distilling crude CH3CN by using three distilling columns having overhead reflux loops of respectively having a reflux ratio higher than (3:1), (3.4:1) and (6.4:1), in turn, under ≥1 atm., to remove HCN and generating a bottom product containing (A) a CH3CN/ water azeotropic mixture and water, separating the component A to (B) a CH3CN/water azeotropic mixture having a higher CH3CN concentration and a bottom product containing water under ≤1 atm., distilling the component B under a pressure of ≥1 atm., then generating a CH3CN/water azeotropic mixture containing substantially whole amount of water derived from the component B, a bottom product containing CH3CN and heavy organic compounds, and a side stream containing (C) a highly purified CH3CN, thus purifying the component C by an acidic ion exchange resin.;COPYRIGHT: (C)1999,JPO
机译:解决的问题:通过将粗制的乙腈作为副产物在丙烯腈生产中进行蒸馏和离子交换树脂处理,从而以较少的工艺获得低成本的高纯度乙腈,可用于色谱法。 ;解决方案:目标化合物是通过使用三个蒸馏塔蒸馏粗制的CH 3 CN来获得的,三个蒸馏塔的塔顶回流回路的回流比分别高于(3:1),(3.4:1)和(6.4:1),然后在≥1atm。下除去HCN,并生成含有(A)CH 3 CN /水共沸混合物和水的底部产物,将组分A分离为(B)CH 3 CN /水共沸混合物,CH 3 CN浓度较高,塔底产物的水含量≤1atm。压力≥1个大气压,然后生成CH 3 CN /水共沸混合物,其中基本上全部成分的水都来自组分B,底部产物中含有CH 3 CN和重有机化合物,以及含有(C)高度纯化的CH 3 CN的侧流,从而通过酸性离子交换树脂纯化组分C 。;版权所有:(C)1999,JPO

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