Batch reactor control using a multiple model-based controller design
This work presents the development of a model‐based controller design called Multiple Model Predictive Control (MMPC) based on a set of linear, time‐varying, state space models to regulate batch processes according to multiple, pre‐specified reference profiles. Sufficient conditions for stability an...
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| Veröffentlicht in: | Canadian journal of chemical engineering 1998-08, Vol.76 (4), p.806-815 |
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| container_title | Canadian journal of chemical engineering |
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| creator | Krishnan, Arun Kosanovich, Karlene A. |
| description | This work presents the development of a model‐based controller design called Multiple Model Predictive Control (MMPC) based on a set of linear, time‐varying, state space models to regulate batch processes according to multiple, pre‐specified reference profiles. Sufficient conditions for stability and boundedness of the dynamic evolution of the forced nonlinear system are provided. The performance of the MMPC design is demonstrated on a model of a batch reactor that represents the production of a polymer product.
On présente dans ce travail la conception d'un régulateur basé sur les modèles appelé Contrôle prédictif de modèles multiples (MMPC), qui s'appuie sur un ensemble de modèles d'espace d'état linéaires et variant dans le temps, afin de réguler des procédés discontinus selon des profils de référence multiples spécifiés préalablement. Des conditions suffisantes sont fournies pour la stabilité et les limites de l'évolution dynamique du système non linéaire forcé. On démontre la performance du MMPC sur un modèle de réacteur discontinu qui représente la production d'un polymère. |
| doi_str_mv | 10.1002/cjce.5450760417 |
| format | Article |
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On présente dans ce travail la conception d'un régulateur basé sur les modèles appelé Contrôle prédictif de modèles multiples (MMPC), qui s'appuie sur un ensemble de modèles d'espace d'état linéaires et variant dans le temps, afin de réguler des procédés discontinus selon des profils de référence multiples spécifiés préalablement. Des conditions suffisantes sont fournies pour la stabilité et les limites de l'évolution dynamique du système non linéaire forcé. On démontre la performance du MMPC sur un modèle de réacteur discontinu qui représente la production d'un polymère.</description><identifier>ISSN: 0008-4034</identifier><identifier>EISSN: 1939-019X</identifier><identifier>DOI: 10.1002/cjce.5450760417</identifier><identifier>CODEN: CJCEA7</identifier><language>eng</language><publisher>Hoboken: Wiley Subscription Services, Inc., A Wiley Company</publisher><subject>Applied sciences ; batch reactors ; Chemical engineering ; Computer science; control theory; systems ; Control theory. Systems ; Exact sciences and technology ; moving horizon control ; multiple models ; Organic polymers ; Physicochemistry of polymers ; Polymerization ; Preparation, kinetics, thermodynamics, mechanism and catalysts ; Process control. Computer integrated manufacturing ; Reactors</subject><ispartof>Canadian journal of chemical engineering, 1998-08, Vol.76 (4), p.806-815</ispartof><rights>Copyright © 1998 Canadian Society for Chemical Engineering</rights><rights>1998 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c4267-574892f173a90809bfb7fa49aff3b699a0cc9ebda4d67d13b1ccddccaca2a753</citedby><cites>FETCH-LOGICAL-c4267-574892f173a90809bfb7fa49aff3b699a0cc9ebda4d67d13b1ccddccaca2a753</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Fcjce.5450760417$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Fcjce.5450760417$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,780,784,1417,27924,27925,45574,45575</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=2415903$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Krishnan, Arun</creatorcontrib><creatorcontrib>Kosanovich, Karlene A.</creatorcontrib><title>Batch reactor control using a multiple model-based controller design</title><title>Canadian journal of chemical engineering</title><addtitle>Can. J. Chem. Eng</addtitle><description>This work presents the development of a model‐based controller design called Multiple Model Predictive Control (MMPC) based on a set of linear, time‐varying, state space models to regulate batch processes according to multiple, pre‐specified reference profiles. Sufficient conditions for stability and boundedness of the dynamic evolution of the forced nonlinear system are provided. The performance of the MMPC design is demonstrated on a model of a batch reactor that represents the production of a polymer product.
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On présente dans ce travail la conception d'un régulateur basé sur les modèles appelé Contrôle prédictif de modèles multiples (MMPC), qui s'appuie sur un ensemble de modèles d'espace d'état linéaires et variant dans le temps, afin de réguler des procédés discontinus selon des profils de référence multiples spécifiés préalablement. Des conditions suffisantes sont fournies pour la stabilité et les limites de l'évolution dynamique du système non linéaire forcé. On démontre la performance du MMPC sur un modèle de réacteur discontinu qui représente la production d'un polymère.</abstract><cop>Hoboken</cop><pub>Wiley Subscription Services, Inc., A Wiley Company</pub><doi>10.1002/cjce.5450760417</doi><tpages>10</tpages></addata></record> |
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| subjects | Applied sciences batch reactors Chemical engineering Computer science control theory systems Control theory. Systems Exact sciences and technology moving horizon control multiple models Organic polymers Physicochemistry of polymers Polymerization Preparation, kinetics, thermodynamics, mechanism and catalysts Process control. Computer integrated manufacturing Reactors |
| title | Batch reactor control using a multiple model-based controller design |
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