MPC of distillation column with side reactors for methyl acetate

Cuimei Bo; Jun Li; Lei Yang; Hui Yi; Jihai Tang; Xu Qiao

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MPC of distillation column with side reactors for methyl acetate

第25届中国过程控制会议专栏 | Updated：2026-01-06

- MPC of distillation column with side reactors for methyl acetate
- Chinese Journal of Chemical Engineering Vol. 25, Issue 12, Pages: 1798-1804(2017)
- Affiliations：
  
  State Key Laboratory of Materials-oriented Chemical Engineering, Nanjing Tech University,Nanjing,China,210009
- Author bio：
- Funds：
- DOI：
  CLC：
- Published：2017
- Accepted：
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Cuimei Bo, Jun Li, Lei Yang, Hui Yi, Jihai Tang, Xu Qiao. MPC of distillation column with side reactors for methyl acetate[J]. Chin.J.Chem.Eng., 2017, 25(12): 1798-1804.
DOI：

Cuimei Bo, Jun Li, Lei Yang, Hui Yi, Jihai Tang, Xu Qiao. MPC of distillation column with side reactors for methyl acetate[J]. Chin.J.Chem.Eng., 2017, 25(12): 1798-1804. DOI：

摘要

Abstract

This paper focuses on the dynamic control of distillation columnwith side reactors (SRC) formethyl acetate production. To obtain the optimumintegrated structure and steady state simulation

the systematic design approach based on the concept of independent reaction amount is applied to the process of SRC formethyl acetate production. In addition to the basic control loops

multi-variable model predictive control modular with methyl acetate concentration and temperature of sensitive plate is designed. Then

based on process simulation software Aspen Plus

dynamic simulation of SRC for methyl acetate production is used to verify the effectiveness of the control scheme.

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