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

• 研究论文 • 上一篇    下一篇

PTA醋酸甲酯水解过程厂级稳态模拟与集成优化

黄燕1, 薄翠梅1, 管国锋2, 丁帅1   

  1. 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
  • 收稿日期:2015-12-24 修回日期:2016-01-05 出版日期:2016-03-05 发布日期:2016-01-12
  • 通讯作者: 薄翠梅
  • 基金资助:

    国家自然科学基金项目(61203020,21276126);江苏省自然科学基金项目(BK20141461)。

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

HUANG Yan1, BO Cuimei1, GUAN Guofeng2, DING Shuai1   

  1. 1. College of Electrical Engineering and Control Science, Nanjing Tech University, Nanjing 211816, Jiangsu, China;
    2. College of Chemistry and Chemical Engineering, Nanjing Tech University, Nanjing 211816, Jiangsu, China
  • Received:2015-12-24 Revised:2016-01-05 Online:2016-03-05 Published:2016-01-12
  • Contact: 67
  • Supported by:

    supported by the National Natural Science Foundation of China (61203020, 21276126) and the Natural Science Foundation of Jiangsu Province (BK20141461).

摘要:

针对PTA生产过程中副产物醋酸甲酯水解回收工艺,利用Aspen Plus软件进行厂级稳态流程模拟与集成优化设计。首先分析水解工艺的热力学、动力学性质,建立水解工艺稳态流程模拟结构,与实际生产数据对比分析验证稳态模拟结果的正确性;其次采用序贯优化法,以年生产成本最小化为目标,对工艺结构和操作参数进行优化,使工艺达到最佳操作条件且生产成本最低。

关键词: 醋酸甲酯水解, 反应精馏, 优化设计, 稳态模拟

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.

Key words: hydrolysis of methyl acetate, reactive distillation, optimization design, steady-state simulation

中图分类号: