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稳态目标优化的稳定MIMO约束预测控制
引用本文:黄德先,王京春,金以慧.稳态目标优化的稳定MIMO约束预测控制[J].中国化学工程学报,2000,8(4):332-338.
作者姓名:黄德先  王京春  金以慧
作者单位:DepartmentofAutomation,TsinghuaUniversity,Beijing100084Cllina
基金项目:Supported by the National Natrural Science Foundation of China(No.69635010).
摘    要:A two-stage multi-objective optimization model-predictive control algorithms(MPC) strategy is presented. A domain MPC controller with input constraints is used to increase freedom for steady-state objective and enhance stabilization of the controller. A steady-state objective optimization algorithm oriented to transient process is adopted to realize optimization of objectives else than dynamic control. It is proved that .the stabilization for both dynamic control and steady-state objective optimization can be guaranteed. The theoretical results are demonstrated and discussed using a distillation tower as the model. Theoretical analysis and simulation results show that this control stratek--v is efl$cient and provides a good strategic solution to uractical urocess control.

关 键 词:稳态目标优化  稳定性  MIMO  约束机制  预测控制  化工过程控制  物料输送
修稿时间: 

Stable MIMO Constrained Predictive Control with Steady state Objective Optimization
HUANG Dexian,WANG Jingchun,JIN Yihui.Stable MIMO Constrained Predictive Control with Steady state Objective Optimization[J].Chinese Journal of Chemical Engineering,2000,8(4):332-338.
Authors:HUANG Dexian  WANG Jingchun  JIN Yihui
Affiliation:Department of Automation, Tsinghua University, Beijing 100084 China
Abstract:A two-stage multi-objective optimization model-predictive control algorithms(MPC) strategy is presented. A domain MPC controller with input constraints is used to increase freedom for steady-state objective and enhance stabilization of the controller. A steady-state objective optimization algorithm oriented to transient process is adopted to realize optimization of objectives else than dynamic control. It is proved that the stabilization for both dynamic control and steady-state objective optimization can be guaranteed. The theoretical results are demonstrated and discussed using a distillation tower as the model. Theoretical analysis and simulation results show that this control strategy is efficient and provides a good strategic solution to practical process control.
Keywords:predictive control  constraint control  optimization  stability  
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