Control of a solution copolymerization reactor using multi-model predictive control

Leyla Özkan, Mayuresh V. Kothare, Christos Georgakis

Research output: Contribution to journalArticle

Abstract

We study the control of a solution copolymerization reactor using a model predictive control algorithm based on multiple piecewise linear models. The control algorithm is a receding horizon scheme with a quasi-infinite horizon objective function which has finite and infinite horizon cost components and uses multiple linear models in its predictions. The finite horizon cost consists of free input variables that direct the system towards a terminal region which contains the desired operating point. The infinite horizon cost has an upper bound and takes the system to the final operating point. Simulation results on an industrial scale methyl methacrylate vinyl acetate solution copolymerization reactor model demonstrate the ability of the algorithm to rapidly transition the process between different operating points.

Original languageEnglish (US)
Pages (from-to)1207-1221
Number of pages15
JournalChemical Engineering Science
Volume58
Issue number7
DOIs
StatePublished - Apr 2003
Externally publishedYes

Fingerprint

Model predictive control
Copolymerization
Costs
Methacrylates

Keywords

  • Linear matrix inequalities
  • Model predictive control
  • Nonlinear dynamics
  • Polymer
  • Process control
  • System engineering

ASJC Scopus subject areas

  • Chemical Engineering(all)

Cite this

Control of a solution copolymerization reactor using multi-model predictive control. / Özkan, Leyla; Kothare, Mayuresh V.; Georgakis, Christos.

In: Chemical Engineering Science, Vol. 58, No. 7, 04.2003, p. 1207-1221.

Research output: Contribution to journalArticle

Özkan, Leyla ; Kothare, Mayuresh V. ; Georgakis, Christos. / Control of a solution copolymerization reactor using multi-model predictive control. In: Chemical Engineering Science. 2003 ; Vol. 58, No. 7. pp. 1207-1221.
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