TY - JOUR
T1 - The design and control of distillation column with side reactors for chlorobenzene production
AU - Bo, Cuimei
AU - Tang, Jihai
AU - Bai, Yangjin
AU - Qiao, Xu
AU - Ding, Lianghui
AU - Zhang, Shi
PY - 2012/12
Y1 - 2012/12
N2 - 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.
AB - 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.
KW - chlorobenzene production
KW - distillation column with side reactors (SRC)
KW - mechanism models
KW - multivariable control schemes
KW - simulation system
UR - http://www.scopus.com/inward/record.url?scp=84872043666&partnerID=8YFLogxK
U2 - 10.1016/S1004-9541(12)60595-3
DO - 10.1016/S1004-9541(12)60595-3
M3 - 文章
AN - SCOPUS:84872043666
SN - 1004-9541
VL - 20
SP - 1113
EP - 1120
JO - Chinese Journal of Chemical Engineering
JF - Chinese Journal of Chemical Engineering
IS - 6
ER -