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PTA醋酸甲酯水解过程厂级稳态模拟与集成优化

黄燕 薄翠梅 管国锋 丁帅

化工学报2016,Vol.67Issue(3):912-918,7.
化工学报2016,Vol.67Issue(3):912-918,7.DOI:10.11949/j.issn.0438-1157.20151955

PTA醋酸甲酯水解过程厂级稳态模拟与集成优化

Steady-state simulation and integrated optimization of reactive distillation for methyl acetate hydrolysis

黄燕 1薄翠梅 1管国锋 2丁帅1

作者信息

  • 1. 南京工业大学电气工程与控制科学学院,江苏南京 211816
  • 2. 南京工业大学化学化工学院,江苏南京 211816
  • 折叠

摘要

Abstract

For recovery process of methyl acetate hydrolysis, this paper simulated process and designed integrated optimization by using Aspen Plus software. Firstly, analyses of thermodynamic and kinetic properties of the hydrolysis process were given. Secondly, the paper established steady-state process simulation structure of hydrolysis process and verified the accuracy of steady-state results. Then it used sequential optimization method to optimize process structure and operation parameters at the aim of achieving minimum production cost. The results showed that operating condition was the best and production cost was the lowest after optimization.

关键词

醋酸甲酯水解/反应精馏/优化设计/稳态模拟

Key words

hydrolysis of methyl acetate/reactive distillation/optimization design/steady-state simulation

分类

化学化工

引用本文复制引用

黄燕,薄翠梅,管国锋,丁帅..PTA醋酸甲酯水解过程厂级稳态模拟与集成优化[J].化工学报,2016,67(3):912-918,7.

基金项目

国家自然科学基金项目(61203020,21276126);江苏省自然科学基金项目(BK20141461)。@@@@supported by the National Natural Science Foundation of China (61203020,21276126) and the Natural Science Foundation of Jiangsu Province (BK20141461) (61203020,21276126)

化工学报

OA北大核心CSCDCSTPCD

0438-1157

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