Product property and production rate control of styrene polymerization

被引:121
作者
Prasad, V
Schley, M
Russo, LP
Bequette, BW [1 ]
机构
[1] Rensselaer Polytech Inst, Isermann Dept Chem Engn, Troy, NY 12180 USA
[2] BASF AG, D-6700 Ludwigshafen, Germany
[3] ExxonMobil Chem Co, Baytown, TX USA
关键词
multi-rate estimation; nonlinear model predictive control (NMPC); styrene polymerization;
D O I
10.1016/S0959-1524(01)00044-0
中图分类号
TP [自动化技术、计算机技术];
学科分类号
0812 ;
摘要
A multivariable multi-rate nonlinear model predictive control (NMPC) strategy is applied to styrene polymerization. The NMPC algorithm incorporates a multi-rate Extended Kalman Filter (EKF) to handle state variable and parameter estimation. A fundamental model is developed for the styrene polymerization CSTR, and control of polymer properties such as number average molecular weight (NAMW) and polydispersity is considered. These properties characterize the final polymer distribution and are strong indicators of the polymer qualities of interest. Production rate control is also demonstrated. Temperature measurements are available frequently while laboratory measurements of concentration and molecular weight distribution are available infrequently with substantial time delays between sampling and analysis. Observability analysis of the augmented system provides guidelines for the design of the augmented disturbance model for use in estimation using the multi-rate EKF. The observability analysis links measurement sets and corresponding observable disturbance models, and shows that measurements of moments of the polymer distribution are essential for good estimation and control. The CSTR is operated at an open-loop unstable steady state. Control simulations are performed under conditions of plant-model structural mismatch and in the presence of parameter uncertainty and disturbances, and the proposed multi-rate NMPC algorithm is shown to provide superior performance compared to linear multi-rate and nonlinear single-rate MPC algorithms. The major contributions of this work are the development of the multi-rate estimator and the measurement design study based on the observability analysis. (C) 2002 Published by Elsevier Science Ltd.
引用
收藏
页码:353 / 372
页数:20
相关论文
共 37 条
[1]   NONLINEAR PREDICTIVE CONTROL USING MULTIRATE SAMPLING [J].
BEQUETTE, BW .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1991, 69 (01) :136-143
[2]   NONLINEAR CONTROL OF CHEMICAL PROCESSES - A REVIEW [J].
BEQUETTE, BW .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (07) :1391-1413
[3]  
BEQUETTE BW, 1998, NATO ASI SER, VE, P3
[4]   NONLINEAR MODEL-BASED CONTROL USING 2ND-ORDER VOLTERRA MODELS [J].
DOYLE, FJ ;
OGUNNAIKE, BA ;
PEARSON, RK .
AUTOMATICA, 1995, 31 (05) :697-714
[5]  
DUERKSEN JH, 1968, J POLYM SCI C, V25, P155
[6]   FEEDBACK-CONTROL OF CHEMICAL PROCESSES USING ONLINE OPTIMIZATION TECHNIQUES [J].
EATON, JW ;
RAWLINGS, JB .
COMPUTERS & CHEMICAL ENGINEERING, 1990, 14 (4-5) :469-479
[7]  
Garcia CE, 1984, AICHE ANN M SAN FRAN
[8]   NONLINEAR QUADRATIC DYNAMIC MATRIX CONTROL WITH STATE ESTIMATION [J].
GATTU, G ;
ZAFIRIOU, E .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1992, 31 (04) :1096-1104
[9]   Verification of controllers in the presence of uncertainty: Application to styrene polymerization [J].
Gazi, E ;
Seider, WD ;
Ungar, LH .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (07) :2277-2287
[10]  
HENDERSON JN, 1979, ACS S SERIES, V104