Simulation Studies on Recovery of Acetonitrile from Aqueous Acetonitrile Waste from Pharmaceutical Processes

S. Tasleem, Satish Kumar Bomma
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Abstract

This paper presents simulation studies on the recovery of Acetonitrile from aqueous Acetonitrile waste from pharmaceutical processes. The focus is on atmospheric distillation in two sequential columns to understand the separation feasibility of the system; the first column produces a distillate of azeotropic composition, which is mixed with a fresh stream and fed to a second column, which produces a 99.9% pure Acetonitrile in the residue. The effect of reflux ratio, reboiler duty and the fresh stream flowrate on the purity of the product is analyzed. The study was performed using steady state simulator Aspen Plus, version 11.1. The simulation results indicate that it is possible to obtain a product of 99.9% w/w Acetonitrile from a 1:1 feed with a recovery of ~ 60%.
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从制药废水中回收乙腈的模拟研究
本文对从制药过程中产生的乙腈废液中回收乙腈进行了模拟研究。重点是常压精馏在两个顺序塔,以了解分离系统的可行性;第一塔产生共沸组分的馏出物,将其与新鲜液混合并送入第二塔,在残留物中产生纯度为99.9%的乙腈。分析了回流比、再沸器负荷和鲜流流量对产品纯度的影响。该研究使用稳态模拟器Aspen Plus 11.1版本进行。模拟结果表明,在1:1的进料条件下,可以获得99.9% w/w的乙腈产品,回收率约为60%。
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