Constraint handing and stability properties of model‐predictive control

Effects of hard constraints in the stability of model-predictive control (MPC) are reviewed. Assuming a fixed active set, the optimal solution can be expressed in a general state-feedback closed form, which corresponds to a piecewise linear controller for the linear model case. Changes in the original unconstrained solution by the active constraints and other effects related to the loss of degrees of freedom are depicted in this analysis. In addition to modifications in the unconstrained feedback gain, we show that the presence of active output constraints can introduce extra feedback terms in the predictive controller. This can lead to instability of the constrained closed-loop system with certain active sets, independent of the choice of tuning parameters. To cope with these problems and extent the constraint handling capabilities of MPC, we introduce the consideration of soft constraints. We compare the use of the l 2 -(quadratic), l 1 -(exact), and l∞-norm penalty formulations. The analysis reveals a strong similarity between the control laws, which allows a direct extrapolation of the unconstrained tuning guidelines to the constrained case. In particular, the exact penalty treatment has identical stability characteristics to the correspondent unconstrained case and therefore seems well suited for general soft constraint handling, even with nonlinear models. These extensions are included in the previously developed Newton control framework, allowing the use of the approach within a consistent framework for both linear and nonlinear process models, increasing the scope of applications of the method. Process examples illustrate the capabilities of the proposed approaches

[1]  Manfred Morari,et al.  Robust Model Predictive Control , 1987, 1987 American Control Conference.

[2]  Lawrence S. Kroll Mathematica--A System for Doing Mathematics by Computer. , 1989 .

[3]  N. L. Ricker,et al.  Case studies of model-predictive control in pulp and paper production , 1988 .

[4]  Wooyoung Lee,et al.  Number of Steady-State Operating Points and Local Stability of Open-Loop Fluid Catalytic Cracker , 1973 .

[5]  John C. Doyle,et al.  Let’s Get Real , 1995 .

[6]  Evanghelos Zafiriou,et al.  Robust Model Predictive Control of Processes with Hard Constraints. , 1990 .

[7]  R. K. Wood,et al.  Terminal composition control of a binary distillation column , 1973 .

[8]  W. C. Li,et al.  Newton-type control strategies for constrained nonlinear processes , 1989 .

[9]  C. Economou An operator theory approach to nonlinear controller design , 1986 .

[10]  John A. Borrie Modern Control Systems: A Manual of Design Methods , 1986 .

[11]  Stephen P. Boyd,et al.  Global Optimization in Control System Analysis and Design , 1992 .

[12]  Evanghelos Zafiriou On the Closed-Loop Stability of Constrained QDMC , 1991, 1991 American Control Conference.

[13]  Chi-Tsong Chen,et al.  Linear System Theory and Design , 1995 .

[14]  R. Varga,et al.  Proof of Theorem 4 , 1983 .

[15]  Manfred Morari,et al.  ∞-norm formulation of model predictive control problems , 1986, 1986 American Control Conference.

[16]  H. Michalska,et al.  Receding horizon control of nonlinear systems , 1988, Proceedings of the 28th IEEE Conference on Decision and Control,.