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Hindawi Publishing Corporation Journal of Control Science and Engineering Volume 2012, Article ID 240898, 2 pages doi:10.1155/2012/240898 Editorial Model Predictive Control Baocang Ding, 1 Marcin T. Cychowski, 2 Yugeng Xi, 3 Wenjian Cai, 4 and Biao Huang 5 1 Ministry of Education Key Lab For Intelligent Networks and Network Security (MOE KLINNS Lab), Department of Automation, School of Electronic and Information Engineering, Xi’an Jiaotong University, Xi’an 710049, China 2 NIMBUS Centre for Embedded Systems Research, Cork Institute of Technology, Rossa Avenue, Cork, Ireland 3 Department of Automation, Shanghai Jiaotong University, Shanghai 200240, China 4 School of Electronic and Electrical Engineering, Nanyang Technological University, BLK S2, Singapore 639798 5 Department of Chemical and Materials Engineering, University of Alberta, Edmonton, AB, Canada T6G 2G6 Correspondence should be addressed to Baocang Ding, [email protected] Received 9 February 2012; Accepted 9 February 2012 Copyright © 2012 Baocang Ding et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited. Model predictive control (MPC) has been a leading technol- ogy in the field of advanced process control for over 30 years. At each sampling time, MPC optimizes a performance cost satisfying the physical constraints, which is initialized by the real measurements, to obtain a sequence of control moves or control laws. However, MPC only implements the control move corresponding to the current sampling time. At the next sampling time, the same optimization problem is solved with renewed initialization. In order to obtain oset-free control, the system model is augmented with a disturbance model to capture the eect of model-pant mismatch. The state and disturbance estimates are utilized to initialize the optimization problem. A steady-state target calculation unit is constructed to compromise between what is desired by real-time optimization (RTO) and what is feasible for the dynamic control move optimization. As a result, MPC ex- hibits innumerous research issues from both theoretical and practical aspects. Nowadays, there is big gap between the theoretical investigations and industrial applications. The main focus of this special issue is on the new research ideas and results for MPC. A total number of 14 papers were submitted for this spe- cial issue. Out of the submitted papers, 6 contributions have been included in this special issue. The 6 papers consider 6 rather dierent, yet interesting topics. A synthesis approach of MPC is the one with guaranteed stability. The technique of linear matrix inequality (LMI) is often used in the synthesis approach to address the satis- faction of physical constraints. However, the existing LMI formulations are for symmetric constraints. M. S. M. Cavalca et al. treat asymmetric output constraints in integrating SISO systems based on pseudoreferences. Usually, the steady-state target calculation, followed with the dynamic move calculation, is implemented in each sam- pling time. This is not practical for fast-sampling systems. Y. C. Chu and M. Z. Q. Chen propose a method to tackle this issue. In their method, the steady-state target calculation works in parallel to, with a period longer than and a scale of optimization larger than, the dynamic move calculation. It is shown that their method is particularly suitable for tracking the periodic references. The nonlinear system represented by a Hammerstein model has always been a good platform for control algorithm research. D. F. He and L. Yu revisit this topic by invoking the pole-placement method on the linear subsystem. They propose the algorithm which consists of three online steps, instead of the two-step MPC. They also propose to use their algorithm in the grade transition control of industrial polypropylene plants, via a simulation study. Usually, MPC has its own paradigm for robust control. However, combing MPC with H 2 / H control could be a good topic for improving the robustness of MPC. P. E. Orukpe applies the mixed H 2 / H method in MPC where the system uncertainties are modeled by perturbations in a linear fractional transform (LFT) representation and unknown bounded disturbances. Interests in the cooperative control of multi-agent sys- tems have been growing significantly over the last years. MPC has the ability to redefine cost functions and constraints as needed to reflect changes in the environment, which makes
Transcript

Hindawi Publishing CorporationJournal of Control Science and EngineeringVolume 2012, Article ID 240898, 2 pagesdoi:10.1155/2012/240898

Editorial

Model Predictive Control

Baocang Ding,1 Marcin T. Cychowski,2 Yugeng Xi,3 Wenjian Cai,4 and Biao Huang5

1 Ministry of Education Key Lab For Intelligent Networks and Network Security (MOE KLINNS Lab),Department of Automation, School of Electronic and Information Engineering, Xi’an Jiaotong University, Xi’an 710049, China

2 NIMBUS Centre for Embedded Systems Research, Cork Institute of Technology, Rossa Avenue, Cork, Ireland3 Department of Automation, Shanghai Jiaotong University, Shanghai 200240, China4 School of Electronic and Electrical Engineering, Nanyang Technological University, BLK S2, Singapore 6397985 Department of Chemical and Materials Engineering, University of Alberta, Edmonton, AB, Canada T6G 2G6

Correspondence should be addressed to Baocang Ding, [email protected]

Received 9 February 2012; Accepted 9 February 2012

Copyright © 2012 Baocang Ding et al. This is an open access article distributed under the Creative Commons Attribution License,which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

Model predictive control (MPC) has been a leading technol-ogy in the field of advanced process control for over 30 years.At each sampling time, MPC optimizes a performance costsatisfying the physical constraints, which is initialized by thereal measurements, to obtain a sequence of control movesor control laws. However, MPC only implements the controlmove corresponding to the current sampling time. At thenext sampling time, the same optimization problem is solvedwith renewed initialization. In order to obtain offset-freecontrol, the system model is augmented with a disturbancemodel to capture the effect of model-pant mismatch. Thestate and disturbance estimates are utilized to initialize theoptimization problem. A steady-state target calculation unitis constructed to compromise between what is desired byreal-time optimization (RTO) and what is feasible for thedynamic control move optimization. As a result, MPC ex-hibits innumerous research issues from both theoretical andpractical aspects. Nowadays, there is big gap between thetheoretical investigations and industrial applications. Themain focus of this special issue is on the new research ideasand results for MPC.

A total number of 14 papers were submitted for this spe-cial issue. Out of the submitted papers, 6 contributions havebeen included in this special issue. The 6 papers consider 6rather different, yet interesting topics.

A synthesis approach of MPC is the one with guaranteedstability. The technique of linear matrix inequality (LMI) isoften used in the synthesis approach to address the satis-faction of physical constraints. However, the existing LMIformulations are for symmetric constraints. M. S. M. Cavalca

et al. treat asymmetric output constraints in integrating SISOsystems based on pseudoreferences.

Usually, the steady-state target calculation, followed withthe dynamic move calculation, is implemented in each sam-pling time. This is not practical for fast-sampling systems.Y. C. Chu and M. Z. Q. Chen propose a method to tacklethis issue. In their method, the steady-state target calculationworks in parallel to, with a period longer than and a scale ofoptimization larger than, the dynamic move calculation. It isshown that their method is particularly suitable for trackingthe periodic references.

The nonlinear system represented by a Hammersteinmodel has always been a good platform for control algorithmresearch. D. F. He and L. Yu revisit this topic by invokingthe pole-placement method on the linear subsystem. Theypropose the algorithm which consists of three online steps,instead of the two-step MPC. They also propose to usetheir algorithm in the grade transition control of industrialpolypropylene plants, via a simulation study.

Usually, MPC has its own paradigm for robust control.However, combing MPC with H2/H∞ control could be agood topic for improving the robustness of MPC. P. E.Orukpe applies the mixed H2/H∞ method in MPC where thesystem uncertainties are modeled by perturbations in a linearfractional transform (LFT) representation and unknownbounded disturbances.

Interests in the cooperative control of multi-agent sys-tems have been growing significantly over the last years. MPChas the ability to redefine cost functions and constraints asneeded to reflect changes in the environment, which makes

2 Journal of Control Science and Engineering

it a nice choice for multiagent systems. S. B. Wei et al. givea method for distributed MPC which punishes, in the costfunction, the deviation between what an agent optimizes andwhat other related agents think of it. The deviation weightmatrix at the end of the control horizon is specially discussedfor improving the control performance.

Besides, C. H. F. Silva et al. report some experimentalstudies for two classical algorithms: infinite horizon MPCand MPC with reference system. The pilot plant is for leveland pH control, which has physical constraints and nonlin-ear dynamics.

We hope the readers of Journal of Control Science andEngineering will find the special issue interesting and stim-ulating, and expect that the included papers contribute tofurther advance the area of MPC.

Acknowledgments

We would like to thank all the authors who have submittedpapers to the special issue and the reviewers involved in therefereeing of the submissions.

Baocang DingMarcin T. Cychowski

Yugeng XiWenjian CaiBiao Huang

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