4.1 Article

A Scheduling and Nonlinear Model Predictive Control Strategy for Continuous Polymerization Reactors

期刊

MACROMOLECULAR REACTION ENGINEERING
卷 8, 期 4, 页码 347-357

出版社

WILEY-V C H VERLAG GMBH
DOI: 10.1002/mren.201300141

关键词

control; dynamics; MINLP; optimization; scheduling

资金

  1. Chair of Process Dynamics and Operation (Dynamik und Betrieb technischer Anlagen Institut fur Prozess und Verfahrenstechnik) at the Technical University of Berlin, Germany

向作者/读者索取更多资源

A novel formulation for addressing planning, scheduling, and control problems in a Methyl-Methacrylate CSTR is presented. Improved optimal solutions can be obtained by using a simultaneous solution approach where the interactions among these problems are explicitly taken into account, in contrast with the classical sequential or decoupled way to address it. In previous works a cyclic production strategy for addressing production patterns has been used. For real-time implementation an extended-horizon production strategy has been used. Moreover, the open-loop optimal dynamic transition trajectories among target polymerization grades are closed-loop implemented using a Nonlinear Model Predictive Control strategy for dealing with disturbance rejection and set-point tracking issues.

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