Inferential Control of Reactive Destillation Columns - An Algorithmic Approach

被引:5
|
作者
Paramasivan, Ganesh [1 ]
Kienle, Achim [1 ,2 ]
机构
[1] Max Planck Inst Dynam Komplexer Tech Syst, D-39106 Magdeburg, Germany
[2] Otto von Guericke Univ, Lehrstuhl Automatisierungstech Modellbildung, Magdeburg, Germany
关键词
Control structure selection; Decentralized control system; Mixed-integer dynamic optimization; Reactive distillation control; DISTILLATION COLUMN; OPTIMIZATION; DESIGN;
D O I
10.1002/ceat.201100141
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Decentralized control system design comprises the selection of a suitable control structure and controller parameters. Here, mixed integer optimization is used to determine the optimal control structure and the optimal controller parameters simultaneously. The process dynamics is included explicitly into the constraints using a rigorous nonlinear dynamic process model. Depending on the objective function, which is used for the evaluation of competing control systems, two different formulations are proposed which lead to mixed-integer dynamic optimization (MIDO) problems. A MIDO solution strategy based on the sequential approach is adopted in the present paper. Here, the MIDO problem is decomposed into a series of nonlinear programming (NLP) subproblems (dynamic optimization) where the binary variables are fixed, and mixed-integer linear programming (MILP) master problems which determine a new binary configuration for the next NLP subproblem. The proposed methodology is applied to inferential control of reactive distillation columns as a challenging benchmark problem for chemical process control.
引用
收藏
页码:1235 / 1244
页数:10
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