The Design and Control of Distillation Column with Side Reactors for Chlorobenzene Production<sup>*</sup>

薄翠梅; 汤吉海; 柏杨进; 乔旭; 丁良辉; 张湜

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The Design and Control of Distillation Column with Side Reactors for Chlorobenzene Production^*

Updated：2026-01-06

- The Design and Control of Distillation Column with Side Reactors for Chlorobenzene Production^*
- The Design and Control of Distillation Column with Side Reactors for Chlorobenzene Production^*
- 中国化学工程学报（英文版） 2012年20卷第6期页码：1113-1120
- Affiliations：
  
  1. College of Automation and Electrical Engineering, Nanjing University of Technology,Nanjing,China,210009
  2. State Key Laboratory of Materials-oriented Chemical Engineering, Nanjing University of Technology,Nanjing,China,210009
- Author bio：
- Funds：
  
  Supported by the National Natural Science Foundation of China (61203020;21276126);the Natural Science Foundation of Jiangsu Province (BK2011795);Jiangsu Province Higher Education Natural Science Foundation (09KJA530004);China Postdoctoral Science Foundation (20100471325)
- DOI：
  中图分类号：
- 纸质出版：2012
- Accepted：
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薄翠梅, 汤吉海, 柏杨进, 等. The Design and Control of Distillation Column with Side Reactors for Chlorobenzene Production^*[J]. 中国化学工程学报（英文版）, 2012,20(6):1113-1120.

[J]. Chinese Journal of Chemical Engineering, 2012, 20(6): 1113-1120.
薄翠梅, 汤吉海, 柏杨进, 等. The Design and Control of Distillation Column with Side Reactors for Chlorobenzene Production^*[J]. 中国化学工程学报（英文版）, 2012,20(6):1113-1120. DOI：

[J]. Chinese Journal of Chemical Engineering, 2012, 20(6): 1113-1120. DOI：

摘要

Abstract

The distillation column with side reactors (SRC) can overcome the temperature/pressure mismatch in the traditional reactive distillation

the column operates at temperature/pressure favorable for vapor-liquid separation

while the reactors operate at temperatures/pressures favorable for reaction kinetics.According to the smooth operation and automatic control problem of the distillation column with side reactors (SRC)

the design

simulation calculation and dynamic control of the SCR process for chlorobenzene production are discussed in the paper.Firstly

the mechanism models

the integrated structure optimal design and process simulation systems are established

respectively.And then multivariable control schemes are designed

the controllability of SRC process based on the optimal steady-state integrated structure is explored.The dynamic response performances of closed-loop system against several disturbances are discussed to verify the effectiveness of control schemes for the SRC process.The simulating results show that the control structure using conventional control strategies can effectively overcome feeding disturbances in a specific range.

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