In this paper, we present a model predictive inferential control (MPIC) strategy to address the problem of controlling unmeasured output variables (such as quality) using readily available secondary measurements. First we establish the relationship between inferential control and other classical control strategies such as cascade and internal model control. Next we present a framework for incorporating the inferential control strategy within the framework of the often used model predictive control (MPC). This framework, termed model predictive inferential control (MPIC), is general enough to accommodate multiple secondary measurements as well as nonlinear estimators and controllers. The advantages of inferential control are established using two case studies. One is the Shell challenge problem which employs linear transfer function models. The second is a nonlinear, multivariable problem on the control of product composition using secondary measurements on a simulated injection pultrusion process. Problems of collinearity are addressed using principal component analysis (PCA) during the construction of the dynamic estimator. These simulations demonstrate the advantages of the proposed model predictive inferential control strategy.
机构:
China Univ Petr East China, Coll Chem Engn, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R ChinaChina Univ Petr East China, Coll Chem Engn, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R China
Wang, Jianxin
Yu, Na
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China Univ Petr East China, Coll Chem Engn, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R ChinaChina Univ Petr East China, Coll Chem Engn, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R China
Yu, Na
Chen, Mengqi
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China Univ Petr East China, Coll Chem Engn, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R ChinaChina Univ Petr East China, Coll Chem Engn, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R China
Chen, Mengqi
Cong, Lin
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China Univ Petr East China, Coll Informat & Control Engn, Qingdao 266580, Peoples R ChinaChina Univ Petr East China, Coll Chem Engn, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R China
Cong, Lin
Sun, Lanyi
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China Univ Petr East China, Coll Chem Engn, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R ChinaChina Univ Petr East China, Coll Chem Engn, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R China
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Arizona State Univ, Dept Chem Bio & Mat Engn, Control Syst Engn Lab, Tempe, AZ 85287 USAArizona State Univ, Dept Chem Bio & Mat Engn, Control Syst Engn Lab, Tempe, AZ 85287 USA
Vargas-Villamil, FD
Rivera, DE
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Arizona State Univ, Dept Chem Bio & Mat Engn, Control Syst Engn Lab, Tempe, AZ 85287 USAArizona State Univ, Dept Chem Bio & Mat Engn, Control Syst Engn Lab, Tempe, AZ 85287 USA
机构:
State Key Laboratory of Heavy Oil Processing, College of Chemical Engineering, China University of Petroleum (East China)State Key Laboratory of Heavy Oil Processing, College of Chemical Engineering, China University of Petroleum (East China)
Jianxin Wang
Na Yu
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State Key Laboratory of Heavy Oil Processing, College of Chemical Engineering, China University of Petroleum (East China)State Key Laboratory of Heavy Oil Processing, College of Chemical Engineering, China University of Petroleum (East China)
Na Yu
Mengqi Chen
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State Key Laboratory of Heavy Oil Processing, College of Chemical Engineering, China University of Petroleum (East China)State Key Laboratory of Heavy Oil Processing, College of Chemical Engineering, China University of Petroleum (East China)
Mengqi Chen
Lin Cong
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College of Information and Control Engineering, China University of Petroleum (East China)State Key Laboratory of Heavy Oil Processing, College of Chemical Engineering, China University of Petroleum (East China)
Lin Cong
Lanyi Sun
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State Key Laboratory of Heavy Oil Processing, College of Chemical Engineering, China University of Petroleum (East China)State Key Laboratory of Heavy Oil Processing, College of Chemical Engineering, China University of Petroleum (East China)