Feasibility of reactive pressure swing batch distillation in a double column configuration

被引：0

作者：

Modla, Gabor ^{[1
]}

机构：

[1] Budapest Univ Technol & Econ, Dept Bldg Serv & Proc Engn, H-1521 Budapest, Hungary

来源：

21ST EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING | 2011年 / 29卷

关键词：

Ethyl-Acetate Production; Reactive Residue Curve Map; Pressure Swing Batch Distillation; Reactive Batch Distillation; Dynamic Simulation; ETHYL;

D O I：

暂无

中图分类号：

TP39 [计算机的应用];

学科分类号：

081203 ; 0835 ;

摘要：

Ethyl-acetate is generally produced by the esterification reaction of ethanol with acetic acid. Since the reaction is equilibrium-limited, the use of reactive distillation is an attractive option. A new double column system is suggested for ethyl-acetate production application of reactive pressure swing batch distillation. The system is investigated by feasibility study based on the analysis of reactive and non-reactive residue curve maps and by rigorous simulation using a professional dynamic simulator.

引用

页码：251 / 255

页数：5

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