Multicriteria dynamic optimization of an emulsion copolymerization reactor
Identifieur interne : 000C00 ( Main/Exploration ); précédent : 000B99; suivant : 000C01Multicriteria dynamic optimization of an emulsion copolymerization reactor
Auteurs : B. Benyahia [France] ; M. A. Latifi [France] ; C. Fonteix [France] ; F. Pla [France]Source :
- Computers & chemical engineering [ 0098-1354 ] ; 2011.
Descripteurs français
- Pascal (Inist)
- Copolymérisation émulsion, Politique optimale, Réacteur chimique, Productivité, Conversion, Transition vitreuse, Système aide décision, Préférence, Théorie utilité, Commande optimale, Styrène, Monomère, Structure coeur couche, Programmation multiobjectif, Programmation dynamique, Algorithme génétique, Algorithme évolutionniste, Modélisation, Minimisation, Optimum Pareto, Prise de décision, Etude expérimentale, Utilité multiattribut.
- Wicri :
- topic : Productivité, Prise de décision.
English descriptors
- KwdEn :
- Chemical reactor, Conversion, Core shell structure, Decision making, Decision support system, Dynamic programming, Emulsion copolymerization, Evolutionary algorithm, Experimental study, Genetic algorithm, Glass transition, Minimization, Modeling, Monomer, Multiattribute utility, Multiobjective programming, Optimal control, Optimal policy, Pareto optimum, Preference, Productivity, Styrene, Utility theory.
- mix :
Abstract
A multicriteria optimization approach based on an evolutionary algorithm has been developed to determine the optimal control policy for a fed-batch emulsion copolymerization reactor, particularly for styrene and butyl acrylate in the presence of n-C12 mercaptan as chain transfer agent. The process model was elaborated and validated experimentally in order to predict the global monomer conversion, the number and weight average molecular weights, the particle size distribution and the residual monomers mass fraction. The process objectives were to produce core-shell particles (hard core and smooth shell) with specific end-use properties and high productivity. This has been achieved by the maximization of the monomers overall conversion at the end of the process and the minimization of the error between the glass transition temperature and a designed profile subject to a set of operational constraints. The nondominated Pareto solutions obtained were ranked according to a decision making aid method based on a decision maker preferences and experience using multi-attribute utility theory. Finally, the best solution was implemented experimentally.
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Affiliations:
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Le document en format XML
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<term>Dynamic programming</term>
<term>Emulsion copolymerization</term>
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<term>Productivity</term>
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<term>Conversion</term>
<term>Transition vitreuse</term>
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<term>Préférence</term>
<term>Théorie utilité</term>
<term>Commande optimale</term>
<term>Styrène</term>
<term>Monomère</term>
<term>Structure coeur couche</term>
<term>Programmation multiobjectif</term>
<term>Programmation dynamique</term>
<term>Algorithme génétique</term>
<term>Algorithme évolutionniste</term>
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<term>Minimisation</term>
<term>Optimum Pareto</term>
<term>Prise de décision</term>
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<term>Core-shell morphology</term>
<term>Decision aid method</term>
<term>Emulsion copolymerization</term>
<term>Experimental implementation</term>
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<front><div type="abstract" xml:lang="en">A multicriteria optimization approach based on an evolutionary algorithm has been developed to determine the optimal control policy for a fed-batch emulsion copolymerization reactor, particularly for styrene and butyl acrylate in the presence of n-C12 mercaptan as chain transfer agent. The process model was elaborated and validated experimentally in order to predict the global monomer conversion, the number and weight average molecular weights, the particle size distribution and the residual monomers mass fraction. The process objectives were to produce core-shell particles (hard core and smooth shell) with specific end-use properties and high productivity. This has been achieved by the maximization of the monomers overall conversion at the end of the process and the minimization of the error between the glass transition temperature and a designed profile subject to a set of operational constraints. The nondominated Pareto solutions obtained were ranked according to a decision making aid method based on a decision maker preferences and experience using multi-attribute utility theory. Finally, the best solution was implemented experimentally.</div>
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