Analysis of intensification mechanism of auxiliary reaction on reactive distillation: Methyl acetate hydrolysis process as example

被引:25
|
作者
Tong, Liwei [1 ,2 ]
Chen, Lifang [1 ,2 ]
Ye, Yinmei [3 ]
Qi, Zhiwen [1 ,2 ]
机构
[1] E China Univ Sci & Technol, State Key Lab Chem Engn, Max Planck Partner Grp, Shanghai 200237, Peoples R China
[2] E China Univ Sci & Technol, Sch Chem Engn, Shanghai 200237, Peoples R China
[3] E China Univ Sci & Technol, Sch Resources & Environm Engn, Shanghai 200237, Peoples R China
基金
中国国家自然科学基金;
关键词
Reactive distillation; Process intensification; Auxiliary reaction; Methyl acetate; Hydrolysis; RESIDUE CURVE MAPS; CATALYTIC DISTILLATION; CHEMICAL-EQUILIBRIUM; DESIGN; KINETICS; CONVERSION; METHANOL;
D O I
10.1016/j.ces.2013.11.036
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A reactive distillation (RD) process directly intensified by an auxiliary reaction is presented. The methyl acetate (MeOAc) hydrolysis intensified by methanol (MeOH) dehydration is studied as an example where the latter serves as the auxiliary reaction. A residue curve maps (RCMs) is developed to analyze the mechanism of intensification for the case with two reactions and multiple components. The analysis of thermodynamics and RCMs reveals that the reaction of MeOH dehydration is the controlling step which limits the conversion of MeOAc. Based on the chemical equilibrium and kinetically controlled design, a novel process is developed to hydrolyze MeOAc and MeOH in the process of polyvinyl alcohol. Compared to traditional processes, no additional water is required to feed into the RD column and the process is significantly simplified. With equal mole of MeOAc and MeOH as teed and a set of pre-reactor, closely 100% conversion of MeOAc and MeOH can be achieved and high purity dimethyl ether and acetic acid are the products in the RD column. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:190 / 197
页数:8
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