DocumentCode :
313176
Title :
Tutorial: process control through nonlinear modeling
Author :
Rhinehart, R. Russell
Author_Institution :
Dept. of Chem. Eng., Texas Tech. Univ., Lubbock, TX, USA
Volume :
3
fYear :
1997
fDate :
4-6 Jun 1997
Firstpage :
2011
Abstract :
Technical advances in computers make it feasible to use nonlinear process models for automatic control. One advantage over linear model-based controllers is that nonlinear controllers are functional over a wider operating range without retuning; and, where process nonlinearity is the major control problem, nonlinear controllers have demonstrated industrial success. When designed with adaptive models, tracking phenomenologically meaningful model coefficients for process diagnosis, and using the model for supervisory optimization are other advantages. Disadvantages are the required case-by-case controller design and inability to mathematically guarantee such features as convergence, stability, etc
Keywords :
control nonlinearities; convergence; dynamics; model reference adaptive control systems; nonlinear control systems; optimisation; process control; SISO systems; convergence; dynamics; model based control; nonlinear control; nonlinear modeling; nonlinearity; process control; process diagnosis; supervisory optimization; Automatic control; Chemical engineering; Difference equations; Industrial control; Inverse problems; Output feedback; Predictive models; Process control; Thermal variables control; Tutorial;
fLanguage :
English
Publisher :
ieee
Conference_Titel :
American Control Conference, 1997. Proceedings of the 1997
Conference_Location :
Albuquerque, NM
ISSN :
0743-1619
Print_ISBN :
0-7803-3832-4
Type :
conf
DOI :
10.1109/ACC.1997.611041
Filename :
611041
Link To Document :
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