Title :
A computationally efficient nonlinear MPC algorithm
Author_Institution :
Dept. of Chem. Eng., Massachusetts Univ., Amherst, MA, USA
Abstract :
In this paper, a novel model predictive control (MPC) algorithm for control of nonlinear multivariable systems is proposed. The online computational demand of the algorithm depends only on the number of manipulated variables; it does not depend on the input (or control) horizon. Thus, the online computational demand is significantly smaller than conventional nonlinear model predictive control algorithms which attempt to solve the online optimization problems exactly. We show that asymptotic stability can be guaranteed in some cases. Its feasibility for practical implementation is demonstrated on a distillation column dual composition control problem using a rigorous tray-by-tray model (with input horizon of 10)
Keywords :
asymptotic stability; computational complexity; multivariable control systems; nonlinear control systems; predictive control; asymptotic stability; computationally efficient nonlinear MPC algorithm; distillation column dual composition control; model predictive control; nonlinear multivariable systems; online computational demand; online optimization; rigorous tray-by-tray model; Constraint optimization; Control systems; Linear approximation; Nonlinear control systems; Nonlinear systems; Prediction algorithms; Predictive control; Predictive models; Robust stability; Sampling methods;
Conference_Titel :
American Control Conference, 1997. Proceedings of the 1997
Conference_Location :
Albuquerque, NM
Print_ISBN :
0-7803-3832-4
DOI :
10.1109/ACC.1997.610858