DocumentCode
3423599
Title
A variably tuned multiple model predictive controller based on minimal process knowledge
Author
Aufderheide, Brian ; Bequette, B. Wayne
Author_Institution
Dept. of Chem. Eng., Rensselaer Polytech. Inst., Troy, NY, USA
Volume
5
fYear
2001
fDate
2001
Firstpage
3490
Abstract
A multiple model predictive controller is designed using minimal plant knowledge based on the ranges on gains, dominant time constants and time delays. The algorithm uses a weighted multiple model bank of first order plus deadtime models as the prediction model for a constrained model predictive controller. A variable tuning strategy is implemented to improve controller performance. The simulated process I´S the isothermal Van de Vusse reaction in a continuously stirred tank reactor (CSTR); this system exhibits input multiplicities, making it a challenging control problem
Keywords
controllers; delays; optimisation; predictive control; step response; tuning; constrained model predictive controller; continuously stirred tank reactor; controller performance; deadtime models; dominant-time constants; isothermal Van de Vusse reaction; minimal plant knowledge; minimal process knowledge; prediction model; simulated process; time delays; variable tuning strategy; variably tuned multiple model predictive controller; weighted multiple model bank; Chemical reactors; Continuous-stirred tank reactor; Delay effects; Equations; Frequency estimation; Inductors; Nonlinear control systems; Nonlinear dynamical systems; Predictive models; Steady-state;
fLanguage
English
Publisher
ieee
Conference_Titel
American Control Conference, 2001. Proceedings of the 2001
Conference_Location
Arlington, VA
ISSN
0743-1619
Print_ISBN
0-7803-6495-3
Type
conf
DOI
10.1109/ACC.2001.946173
Filename
946173
Link To Document