Nonlinear observer design for process monitoring

被引:51
作者
Kazantzis, N
Kravaris, C
Wright, RA
机构
[1] Univ Michigan, Dept Chem Engn, Ann Arbor, MI 48109 USA
[2] Dow Chem Co USA, Midland, MI 48667 USA
关键词
D O I
10.1021/ie990321n
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The present work proposes a systematic nonlinear observer design framework for process monitoring. The objective is to accurately monitor key process variables associated with process safety or product quality, by designing a model-based nonlinear observer that directly utilizes the available information coming from continuous-time on-line process output measurements. The nonlinear observer possesses a state-dependent gain which is computed from the solution of a system of first-order linear partial differential equations (PDEs). Depending on whether the process operates in continuous or batch made, a different mathematical treatment and solution scheme for the system of PDEs is needed. Within the proposed design framework, both full-order and reduced-order observers are studied. Finally, the performance of the proposed observer is evaluated in two chemical-engineering examples: (1) a catalytic batch reactor where the objective is to accurately estimate the catalyst activity and (2) an exothermic CSTR that exhibits steady-state multiplicity and the heat released by the reaction needs to be closely monitored.
引用
收藏
页码:408 / 419
页数:12
相关论文
共 38 条
[1]   CONTINUOUS SOLUTION POLYMERIZATION REACTOR CONTROL .2. ESTIMATION AND NONLINEAR REFERENCE CONTROL DURING METHYL-METHACRYLATE POLYMERIZATION [J].
ADEBEKUN, DK ;
SCHORK, FJ .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (12) :1846-1861
[2]  
[Anonymous], 1974, APPL OPTIMAL ESTIMAT
[3]  
BASTIN G, 1990, OLINE ESTIMATION ADA
[4]   CANONICAL FORM OBSERVER DESIGN FOR NON-LINEAR TIME-VARIABLE SYSTEMS [J].
BESTLE, D ;
ZEITZ, M .
INTERNATIONAL JOURNAL OF CONTROL, 1983, 38 (02) :419-431
[5]  
Chen C.-T., 1984, LINEAR SYSTEM THEORY
[6]   A LUENBERGER-LIKE OBSERVER FOR NONLINEAR-SYSTEMS [J].
CICCARELLA, G ;
DALLAMORA, M ;
GERMANI, A .
INTERNATIONAL JOURNAL OF CONTROL, 1993, 57 (03) :537-556
[7]  
COURANT R, 1962, METHODS MATH PHYSICS, V2
[8]   NONLINEAR OBSERVER DESIGN VIA AN EXTENDED OBSERVER CANONICAL FORM [J].
DING, XC ;
FRANK, PM ;
GUO, LM .
SYSTEMS & CONTROL LETTERS, 1990, 15 (04) :313-322
[9]   ASYMPTOTIC OBSERVERS FOR STIRRED TANK REACTORS [J].
DOCHAIN, D ;
PERRIER, M ;
YDSTIE, BE .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (15-16) :4167-4177
[10]   Nonlinear inferential control for process applications [J].
Doyle, FJ .
JOURNAL OF PROCESS CONTROL, 1998, 8 (5-6) :339-353