Analytical approach to tuning of model predictive control for first-order plus dead time models

被引:29
作者
Bagheri, Peyman [1 ]
Sedigh, Ali Khaki [1 ]
机构
[1] KN Toosi Univ Technol, Dept Elect & Comp Engn, Ctr Excellence Ind Control, Tehran, Iran
关键词
closed loop systems; optimisation; pole assignment; predictive control; stability; time-varying systems; model predictive control; first-order plus dead time models; MPC; analytical tuning strategy; FOPDT; optimisation problem; pole placement framework; closed-loop stability; maximum achievable performance; higher order plants; STRATEGY;
D O I
10.1049/iet-cta.2012.0934
中图分类号
TP [自动化技术、计算机技术];
学科分类号
0812 ;
摘要
Model predictive control (MPC) is an effective control strategy in the presence of system constraints. The successful implementation of MPC in practical applications requires appropriate tuning of the controller parameters. An analytical tuning strategy for MPC of first-order plus dead time (FOPDT) systems is presented when the constraints are inactive. The available tuning methods are generally based on the user's experience and experimental results. Some tuning methods lead to a complex optimisation problem that provides numerical results for the controller parameters. On the other hand, many industrial plants can be effectively described by FOPDT models, and this model is therefore used to derive analytical results for the MPC tuning in a pole placement framework. Then, the issues of closed-loop stability and possible achievable performance are addressed. In the case of no active constraints, it is shown that for the FOPDT models, control horizons subsequent to two do not improve the achievable performance and control horizon of two provides the maximum achievable performance. Then, MPC tuning for higher order plants approximated by FOPDT models is considered. Finally, simulation results are employed to show the effectiveness of the proposed tuning formulas.
引用
收藏
页码:1806 / 1817
页数:12
相关论文
共 17 条
[1]   On-line tuning strategy for model predictive controllers [J].
Al-Ghazzawi, A ;
Ali, E ;
Nouh, A ;
Zafiriou, E .
JOURNAL OF PROCESS CONTROL, 2001, 11 (03) :265-284
[2]  
[Anonymous], 1997, COMPUTER CONTROLLED
[3]   A generalized predictive controller for a wide class of industrial processes [J].
Bordons, C ;
Camacho, EF .
IEEE TRANSACTIONS ON CONTROL SYSTEMS TECHNOLOGY, 1998, 6 (03) :372-387
[4]  
Camacho E.F., 2007, ADV TK CONT SIGN PRO, DOI 10.1007/978-0-85729-398-5
[5]   Model Predictive Control Tuning by Controller Matching [J].
Di Cairano, Stefano ;
Bemporad, Alberto .
IEEE TRANSACTIONS ON AUTOMATIC CONTROL, 2010, 55 (01) :185-190
[6]   Model Predictive Control Tuning Methods: A Review [J].
Garriga, Jorge L. ;
Soroush, Masoud .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (08) :3505-3515
[7]   Tuning of a tracking multi-parametric predictive controller using local linear analysis [J].
Gerksic, S. ;
Pregelj, B. .
IET CONTROL THEORY AND APPLICATIONS, 2012, 6 (05) :669-679
[8]   TUNING OF MODEL-PREDICTIVE CONTROLLERS FOR ROBUST PERFORMANCE [J].
LEE, JH ;
YU, ZH .
COMPUTERS & CHEMICAL ENGINEERING, 1994, 18 (01) :15-37
[9]   Constrained model predictive control: Stability and optimality [J].
Mayne, DQ ;
Rawlings, JB ;
Rao, CV ;
Scokaert, POM .
AUTOMATICA, 2000, 36 (06) :789-814
[10]   Generalized predictive control and tuning of industrial processes with second order plus dead time models [J].
Neshasteriz, A. R. ;
Sedigh, A. Khaki ;
Sadjadian, H. .
JOURNAL OF PROCESS CONTROL, 2010, 20 (02) :63-72