Skip to main content
Log in

Model predictive control for multivariable unstable processes with constraints on manipulated variables

  • Published:
Korean Journal of Chemical Engineering Aims and scope Submit manuscript

Abstract

The original MPC(Model Predictive Control) algorithm cannot be applied to open loop unstable systems, because the step responses of the open loop unstable system never reach steady states. So when we apply MPC to the open loop unstable systems, first we have to stabilize them by state feedback or output feedback. Then the stabilized systems can be controlled by MPC. But problems such as valve saturation may occur because the manipulated input is the summation of the state feedback output and the MPC output. Therefore, we propose Quadratic Dynamic Matrix Control(QDMC) combined with state feedback as a new method to handle the constraints on manipulated variables for multivariable unstable processes. We applied this control method to a single-input-single-output unstable nonlinear system and a multi-input-multi-output unstable system. The results show that this method is robust and can handle the input constraints explicitly and also its control performance is better than that of others such as well tuned PI control. Linear Quadratic Regulator (LQR) with integral action.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Similar content being viewed by others

References

  1. Åstrom, K.J. and Wittenmark, B.: “Computer Controlled System: Theory and Design”, Prentice-Hall (1984).

  2. Cheng, Chun-Min:Ind. Eng. Chem. Res.,28, 178 (1989).

    Article  CAS  Google Scholar 

  3. Cutler, C. R.: Ph.D. Thesis, U. of Houston (1983).

  4. Cutler, C.R.:ISA Transaction,21, 1 (1982).

    Google Scholar 

  5. Cutler, C. R. and Ramaker, B. L: “Dynamic Matrix Control-A Computer Control Algorithm”, AIChE 86th National Meeting, Apr., (1979).

  6. Deshpande, Pradeep B.: “Distillation Dynamics and Control”, Instrument Society of America, (1985).

  7. Garcia, C. E. and Morshedi, A. M.:Chem. Eng. Commun.,46, 73 (1986).

    Article  CAS  Google Scholar 

  8. Georgiou, A., Georgakis, C. and Luyben, W. L.:Ind. Eng. Chem. Res.,28, 1481 (1989).

    Article  CAS  Google Scholar 

  9. Hidalgo, P. M. and Brosilow, C. B.:Computers and Chem. Eng,13, 481 (1990).

    Article  Google Scholar 

  10. Maurath, P. R., Laub, A. J., Seborg, D. E. and Mellichamp, D. A.:Ind. Eng. Chem. Res.,27, 1204 (1988).

    Article  CAS  Google Scholar 

  11. Ogata, K.: “State Space Analysis of Control Systems”, Prentice-Hall (1967).

  12. Ray, W. H.: “Advanced Process Control”, McGraw-Hill (1981).

Download references

Author information

Authors and Affiliations

Authors

Rights and permissions

Reprints and permissions

About this article

Cite this article

Lee, J.K., Park, S.W. Model predictive control for multivariable unstable processes with constraints on manipulated variables. Korean J. Chem. Eng. 8, 195–202 (1991). https://doi.org/10.1007/BF02707184

Download citation

  • Received:

  • Accepted:

  • Issue Date:

  • DOI: https://doi.org/10.1007/BF02707184

Keywords

Navigation