Performance and stability analysis of LP‐MPC and QP‐MPC cascade control systems
Authors:
- 1 July 1999
- journal article
- process systems-engineering
- Published by Wiley in AIChE Journal
- Vol. 45 (7) , 1521-1534
Abstract
Model predictive control (MPC) is used extensively in industry to optimally control constrained, multivariable processes. For nonsquare systems (with more inputs than outputs), extra degrees of freedom can be used to dynamically drive the process to its economic optimum operating conditions. This is accomplished by cascading a local linear programming (LP) or quadratic programming (QP) controller using steady‐state models. Such a cascade control scheme (LP‐MPC or QP‐MPC) continuously computes and updates the set points used by the lower‐level MPC algorithm. While this methodology has been in use by industry for many years, its properties have not been addressed in the literature. The properties of such cascaded MPC systems are analyzed from the point of view of implementation strategies, stability properties, and economic and dynamic performance. Some theoretical results on stability are derived along with a case study involving the Shell control problem.Keywords
This publication has 19 references indexed in Scilit:
- Results analysis for real-time optimization (RTO): Deciding when to change the plant operationComputers & Chemical Engineering, 1996
- Performance bounds for robust quadratic dynamic matrix control with end conditionAIChE Journal, 1995
- Stability of model predictive control with mixed constraintsIEEE Transactions on Automatic Control, 1995
- Model Accuracy for Economic Optimizing Controllers: The Bias Update CaseIndustrial & Engineering Chemistry Research, 1994
- State estimation based model predictive control applied to shell control problem: a case studyChemical Engineering Science, 1994
- The stability of constrained receding horizon controlIEEE Transactions on Automatic Control, 1993
- QUADRATIC PROGRAMMING SOLUTION OF DYNAMIC MATRIX CONTROL (QDMC)Chemical Engineering Communications, 1986
- Internal model control. 2. Design procedure for multivariable systemsIndustrial & Engineering Chemistry Process Design and Development, 1985
- Internal model control. 3. Multivariable control law computation and tuning guidelinesIndustrial & Engineering Chemistry Process Design and Development, 1985
- Model predictive heuristic controlAutomatica, 1978