TIME-DELAY COMPENSATION FOR NONLINEAR PROCESSES

被引:71
作者
HENSON, MA [1 ]
SEBORG, DE [1 ]
机构
[1] UNIV CALIF SANTA BARBARA,DEPT CHEM & NUCL ENGN,SANTA BARBARA,CA 93106
关键词
D O I
10.1021/ie00030a009
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A new time delay compensation strategy for nonlinear processes is developed and evaluated. Simulation results for a continuous stirred tank reactor demonstrate that the globally linearizing control (GLC) compensation technique can yield poor performance in the presence of unmeasured disturbances and/or plant/model mismatch. A theoretical analysis of a discrete-time version of the GLC predictor indicates that the poor regulatory performance is attributable to ineffective use of the process state variables, which are assumed to be measured. A new discrete-time prediction strategy is developed which provides improved predictions, yet maintains the desirable characteristics of the GLC approach. A continuous-time version of the predictor is combined with an input-output linearizing controller to yield the new time delay compensation strategy. The proposed scheme is computationally efficient and not restricted to open-loop stable processes. Simulation results for the reactor example demonstrate the superior performance and robustness of the proposed compensation strategy as compared to the GLC approach.
引用
收藏
页码:1493 / 1500
页数:8
相关论文
共 26 条
[1]  
ALEVISAKIS G, 1973, INT J CONTROL, V3, P541
[2]  
BARTEE JF, 1989, AICHE ANN M SAN FRAN
[3]   NONLINEAR CONTROL OF CHEMICAL PROCESSES - A REVIEW [J].
BEQUETTE, BW .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (07) :1391-1413
[4]  
BIEGLER LT, 1991, CHEM PROCESS CPC, V4
[5]  
Henson M. A., 1991, Journal of Process Control, V1, P122, DOI 10.1016/0959-1524(91)85001-Y
[6]   THEORETICAL-ANALYSIS OF UNCONSTRAINED NONLINEAR MODEL-PREDICTIVE CONTROL [J].
HENSON, MA ;
SEBORG, DE .
INTERNATIONAL JOURNAL OF CONTROL, 1993, 58 (05) :1053-1080
[7]   INPUT-OUTPUT LINEARIZATION OF GENERAL NONLINEAR PROCESSES [J].
HENSON, MA ;
SEBORG, DE .
AICHE JOURNAL, 1990, 36 (11) :1753-1757
[8]   DESIGN OF RESILIENT PROCESSING PLANTS .5. THE EFFECT OF DEADTIME ON DYNAMIC RESILIENCE [J].
HOLT, BR ;
MORARI, M .
CHEMICAL ENGINEERING SCIENCE, 1985, 40 (07) :1229-1237
[9]  
Isidori A., 1989, NONLINEAR CONTROL SY
[10]   HIGH-PERFORMANCE MULTIVARIABLE CONTROL STRATEGIES FOR SYSTEMS HAVING TIME DELAYS [J].
JEROME, NF ;
RAY, WH .
AICHE JOURNAL, 1986, 32 (06) :914-931