DocumentCode :
2258719
Title :
A two-timescale approach to nonlinear model predictive control
Author :
Buescher, Kevin L. ; Baum, Christopher C.
Author_Institution :
Los Alamos Nat. Lab., NM, USA
Volume :
3
fYear :
1995
fDate :
21-23 Jun 1995
Firstpage :
2250
Abstract :
Model predictive control (MPC) schemes generate controls by using a model to predict the plant´s response to various control strategies. A problem arises when the underlying model is obtained by fitting a general nonlinear function, such as a neural network, to data: an exorbitant amount of data may be required to obtain accurate enough predictions. The authors describe a means of avoiding this problem that involves a simplified plant model which bases its predictions on averages of past control inputs. This model operates on a timescale slower than the rate at which the plant outputs and controls are sampled and updated. Not only does this technique give improved closed-loop performance from the same amount of open-loop data, but it requires far less on-line computation as well. The authors illustrate the usefulness of this two-timescale approach by applying it to a simulated exothermic continuously stirred tank reactor with jacket dynamics
Keywords :
chemical technology; closed loop systems; identification; neural nets; nonlinear control systems; predictive control; process control; closed-loop performance; jacket dynamics; nonlinear model predictive control; simplified plant model; simulated exothermic continuously stirred tank reactor; two-timescale approach; Computational modeling; Control system synthesis; Inductors; Laboratories; Neural networks; Open loop systems; Predictive control; Predictive models; Sampling methods; System identification;
fLanguage :
English
Publisher :
ieee
Conference_Titel :
American Control Conference, Proceedings of the 1995
Conference_Location :
Seattle, WA
Print_ISBN :
0-7803-2445-5
Type :
conf
DOI :
10.1109/ACC.1995.531372
Filename :
531372
Link To Document :
بازگشت