MPC of distillation column with side reactors for methyl acetate

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

doi:10.1016/j.cjche.2017.08.012

MPC of distillation column with side reactors for methyl acetate

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

Nanjing Tech University

Research output: Contribution to journal › Article › peer-review

2 Scopus citations

Abstract

This paper focuses on the dynamic control of distillation column with side reactors (SRC) for methyl acetate production. To obtain the optimum integrated structure and steady state simulation, the systematic design approach based on the concept of independent reaction amount is applied to the process of SRC for methyl 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.

Original language	English
Pages (from-to)	1798-1804
Number of pages	7
Journal	Chinese Journal of Chemical Engineering
DOIs	https://doi.org/10.1016/j.cjche.2017.08.012
State	Published - Dec 2017

Keywords

Distillation column with side reactors (SRC)
Dynamic simulation
Methyl acetate
Multi-variable model predictive control (MPC)
Steady-state optimization

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10.1016/j.cjche.2017.08.012

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title = "MPC of distillation column with side reactors for methyl acetate",

abstract = "This paper focuses on the dynamic control of distillation column with side reactors (SRC) for methyl acetate production. To obtain the optimum integrated structure and steady state simulation, the systematic design approach based on the concept of independent reaction amount is applied to the process of SRC for methyl 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.",

keywords = "Distillation column with side reactors (SRC), Dynamic simulation, Methyl acetate, Multi-variable model predictive control (MPC), Steady-state optimization",

author = "Cuimei Bo and Jun Li and Lei Yang and Hui Yi and Jihai Tang and Xu Qiao",

note = "Publisher Copyright: {\textcopyright} 2017",

year = "2017",

month = dec,

doi = "10.1016/j.cjche.2017.08.012",

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TY - JOUR

T1 - MPC of distillation column with side reactors for methyl acetate

AU - Bo, Cuimei

AU - Li, Jun

AU - Yang, Lei

AU - Yi, Hui

AU - Tang, Jihai

AU - Qiao, Xu

PY - 2017/12

Y1 - 2017/12

N2 - This paper focuses on the dynamic control of distillation column with side reactors (SRC) for methyl acetate production. To obtain the optimum integrated structure and steady state simulation, the systematic design approach based on the concept of independent reaction amount is applied to the process of SRC for methyl 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.

AB - This paper focuses on the dynamic control of distillation column with side reactors (SRC) for methyl acetate production. To obtain the optimum integrated structure and steady state simulation, the systematic design approach based on the concept of independent reaction amount is applied to the process of SRC for methyl 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.

KW - Distillation column with side reactors (SRC)

KW - Dynamic simulation

KW - Methyl acetate

KW - Multi-variable model predictive control (MPC)

KW - Steady-state optimization

UR - http://www.scopus.com/inward/record.url?scp=85033724060&partnerID=8YFLogxK

U2 - 10.1016/j.cjche.2017.08.012

DO - 10.1016/j.cjche.2017.08.012

M3 - 文章

AN - SCOPUS:85033724060

SN - 1004-9541

SP - 1798

EP - 1804

JO - Chinese Journal of Chemical Engineering

JF - Chinese Journal of Chemical Engineering

ER -

MPC of distillation column with side reactors for methyl acetate

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Keywords

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