Nonlinear model predictive control for dividing wall columns

被引:12
作者
Qian, Xing [1 ,2 ]
Lin, Kuan-Han [2 ]
Jia, Shengkun [3 ]
Biegler, Lorenz T. [2 ]
Huang, Kejin [1 ]
机构
[1] Beijing Univ Chem Technol, Coll Informat Sci & Technol, Beijing, Peoples R China
[2] Carnegie Mellon Univ, Chem Engn Dept, Pittsburgh, PA 15213 USA
[3] Tianjin Univ, State Key Lab Chem Engn, Collaborat Innovat Ctr Chem Sci & Engn Tianjin, Sch Chem Engn & Technol,Chem Engn Res Ctr, Beiyangyuan Campus, Yaguan Rd 135, Tianjin 300350, Peoples R China
基金
中国国家自然科学基金;
关键词
distillation; dividing wall column; nonlinear model predictive control; SEPARATION; ALGORITHM;
D O I
10.1002/aic.18062
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Dividing wall columns (DWCs) are practical, effective, and promising among distillation process intensification technologies. Nonlinear model predictive control (NMPC) schemes are developed in this study to control the three-product DWCs. As these systems are intensely interactive and highly nonlinear, NMPC may be more suitable than the traditional PI control. The model is established based on Python and Pyomo platforms. As the original mathematical model of the column section is ill-posed, index reduction is used to avoid a high-index differential-algebraic equation (DAE) system. The well-posed index-1 system after index reduction is employed for the steady-state simulation and dynamic control in this study. Case studies with three DWC configurations to separate the mixture of ethanol (A), n-propanol (B), and n-butanol (C) show that the NMPC performs very well with small maximum deviations and short settling times. This demonstrates that the NMPC is a feasible and very effective scheme to control three-product DWCs.
引用
收藏
页数:22
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