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New Processes For Recovery Of Acetic Acid From Waste Water

机译:从废水中回收乙酸的新工艺

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This paper addresses an industrially important problem of acetic acid recovery from a waste water stream via reactive distillation. The presence of a three-phase regime on the column stages due to a liquid-liquid phase split between aqueous and organic phases is a typical characteristic of this process. A modern modeling approach is presented to detect the existence of potential phase splitting in this column. A good agreement of a phase splitting model with the literature data has been shown. A theoretical study for the recovery of acetic acid from its 30 wt% aqueous solution by esterification with n-butanol is presented. Alternate column structures were investigated and two structures rendering theoretically close to 100% conversion of acetic acid were identified. The dynamic simulations were performed on proposed structures to see transient responses wrt. to common process disturbances.
机译:本文探讨了通过反应蒸馏从废水中回收乙酸的工业重要问题。由于水相和有机相之间的液-液相分离,在柱级上存在三相状态是该方法的典型特征。提出了一种现代建模方法来检测此列中是否存在潜在的相分离。已经显示出相分离模型与文献数据的良好一致性。提出了通过用正丁醇酯化从其30 wt%的水溶液中回收乙酸的理论研究。研究了交替的柱结构,确定了理论上接近100%乙酸转化率的两个结构。在建议的结构上进行了动态仿真,以观察瞬态响应。常见的过程干扰。

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