Simultaneous Design and Control of a Semibatch Styrene Polymerization Reactor

Autores
Asteasuain, Mariano; Brandolin, Adriana; Sarmoria, Claudia; Bandoni, Jose Alberto
Año de publicación
2004
Idioma
inglés
Tipo de recurso
artículo
Estado
versión publicada
Descripción
It has been established that the security, flexibility, and dynamic controllability of a process are inherent properties of its design, which also affects process economics. In this context, we employed a previously developed mixed-integer dynamic optimization (MIDO) approach to perform the simultaneous design and control of styrene polymerization reactors. Industrial- and laboratory-size semibatch jacketed reactors were considered. The gPROMS/gOPT package was successfully used to solve the mixed-integer dynamic optimizations. In each case, the geometry, initiator mixture composition, and control system were optimally determined in a single optimization run. We analyzed the effect of using different coolants with and without heat supply on the laboratory-scale reactor design. We also studied the effect of scale-up in the integrated process and control design. Design coincidences and differences were analyzed.
Fil: Asteasuain, Mariano. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
Fil: Brandolin, Adriana. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
Fil: Sarmoria, Claudia. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
Fil: Bandoni, Jose Alberto. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
Materia
OXIDES
POLIMERIZATION
MIXTURES
FLUIDS
OPTIMIZATION
Nivel de accesibilidad
acceso abierto
Condiciones de uso
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
Repositorio
CONICET Digital (CONICET)
Institución
Consejo Nacional de Investigaciones Científicas y Técnicas
OAI Identificador
oai:ri.conicet.gov.ar:11336/130182
Acceder
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network_name_str CONICET Digital (CONICET)
spelling Simultaneous Design and Control of a Semibatch Styrene Polymerization ReactorAsteasuain, MarianoBrandolin, AdrianaSarmoria, ClaudiaBandoni, Jose AlbertoOXIDESPOLIMERIZATIONMIXTURESFLUIDSOPTIMIZATIONhttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2It has been established that the security, flexibility, and dynamic controllability of a process are inherent properties of its design, which also affects process economics. In this context, we employed a previously developed mixed-integer dynamic optimization (MIDO) approach to perform the simultaneous design and control of styrene polymerization reactors. Industrial- and laboratory-size semibatch jacketed reactors were considered. The gPROMS/gOPT package was successfully used to solve the mixed-integer dynamic optimizations. In each case, the geometry, initiator mixture composition, and control system were optimally determined in a single optimization run. We analyzed the effect of using different coolants with and without heat supply on the laboratory-scale reactor design. We also studied the effect of scale-up in the integrated process and control design. Design coincidences and differences were analyzed.Fil: Asteasuain, Mariano. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; ArgentinaFil: Brandolin, Adriana. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; ArgentinaFil: Sarmoria, Claudia. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; ArgentinaFil: Bandoni, Jose Alberto. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; ArgentinaAmerican Chemical Society2004-08-13info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/130182Asteasuain, Mariano; Brandolin, Adriana; Sarmoria, Claudia; Bandoni, Jose Alberto; Simultaneous Design and Control of a Semibatch Styrene Polymerization Reactor; American Chemical Society; Industrial & Engineering Chemical Research; 43; 17; 13-8-2004; 5233-52470888-5885CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/doi/10.1021/ie040021sinfo:eu-repo/semantics/altIdentifier/url/https://pubs.acs.org/doi/10.1021/ie040021sinfo:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-10-22T11:18:46Zoai:ri.conicet.gov.ar:11336/130182instacron:CONICETInstitucionalhttp://ri.conicet.gov.ar/Organismo científico-tecnológicoNo correspondehttp://ri.conicet.gov.ar/oai/requestdasensio@conicet.gov.ar; lcarlino@conicet.gov.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:34982025-10-22 11:18:46.735CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse
dc.title.none.fl_str_mv Simultaneous Design and Control of a Semibatch Styrene Polymerization Reactor
title Simultaneous Design and Control of a Semibatch Styrene Polymerization Reactor
spellingShingle Simultaneous Design and Control of a Semibatch Styrene Polymerization Reactor
Asteasuain, Mariano
OXIDES
POLIMERIZATION
MIXTURES
FLUIDS
OPTIMIZATION
title_short Simultaneous Design and Control of a Semibatch Styrene Polymerization Reactor
title_full Simultaneous Design and Control of a Semibatch Styrene Polymerization Reactor
title_fullStr Simultaneous Design and Control of a Semibatch Styrene Polymerization Reactor
title_full_unstemmed Simultaneous Design and Control of a Semibatch Styrene Polymerization Reactor
title_sort Simultaneous Design and Control of a Semibatch Styrene Polymerization Reactor
dc.creator.none.fl_str_mv Asteasuain, Mariano
Brandolin, Adriana
Sarmoria, Claudia
Bandoni, Jose Alberto
author Asteasuain, Mariano
author_facet Asteasuain, Mariano
Brandolin, Adriana
Sarmoria, Claudia
Bandoni, Jose Alberto
author_role author
author2 Brandolin, Adriana
Sarmoria, Claudia
Bandoni, Jose Alberto
author2_role author
author
author
dc.subject.none.fl_str_mv OXIDES
POLIMERIZATION
MIXTURES
FLUIDS
OPTIMIZATION
topic OXIDES
POLIMERIZATION
MIXTURES
FLUIDS
OPTIMIZATION
purl_subject.fl_str_mv https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
dc.description.none.fl_txt_mv It has been established that the security, flexibility, and dynamic controllability of a process are inherent properties of its design, which also affects process economics. In this context, we employed a previously developed mixed-integer dynamic optimization (MIDO) approach to perform the simultaneous design and control of styrene polymerization reactors. Industrial- and laboratory-size semibatch jacketed reactors were considered. The gPROMS/gOPT package was successfully used to solve the mixed-integer dynamic optimizations. In each case, the geometry, initiator mixture composition, and control system were optimally determined in a single optimization run. We analyzed the effect of using different coolants with and without heat supply on the laboratory-scale reactor design. We also studied the effect of scale-up in the integrated process and control design. Design coincidences and differences were analyzed.
Fil: Asteasuain, Mariano. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
Fil: Brandolin, Adriana. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
Fil: Sarmoria, Claudia. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
Fil: Bandoni, Jose Alberto. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
description It has been established that the security, flexibility, and dynamic controllability of a process are inherent properties of its design, which also affects process economics. In this context, we employed a previously developed mixed-integer dynamic optimization (MIDO) approach to perform the simultaneous design and control of styrene polymerization reactors. Industrial- and laboratory-size semibatch jacketed reactors were considered. The gPROMS/gOPT package was successfully used to solve the mixed-integer dynamic optimizations. In each case, the geometry, initiator mixture composition, and control system were optimally determined in a single optimization run. We analyzed the effect of using different coolants with and without heat supply on the laboratory-scale reactor design. We also studied the effect of scale-up in the integrated process and control design. Design coincidences and differences were analyzed.
publishDate 2004
dc.date.none.fl_str_mv 2004-08-13
dc.type.none.fl_str_mv info:eu-repo/semantics/article
info:eu-repo/semantics/publishedVersion
http://purl.org/coar/resource_type/c_6501
info:ar-repo/semantics/articulo
format article
status_str publishedVersion
dc.identifier.none.fl_str_mv http://hdl.handle.net/11336/130182
Asteasuain, Mariano; Brandolin, Adriana; Sarmoria, Claudia; Bandoni, Jose Alberto; Simultaneous Design and Control of a Semibatch Styrene Polymerization Reactor; American Chemical Society; Industrial & Engineering Chemical Research; 43; 17; 13-8-2004; 5233-5247
0888-5885
CONICET Digital
CONICET
url http://hdl.handle.net/11336/130182
identifier_str_mv Asteasuain, Mariano; Brandolin, Adriana; Sarmoria, Claudia; Bandoni, Jose Alberto; Simultaneous Design and Control of a Semibatch Styrene Polymerization Reactor; American Chemical Society; Industrial & Engineering Chemical Research; 43; 17; 13-8-2004; 5233-5247
0888-5885
CONICET Digital
CONICET
dc.language.none.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv info:eu-repo/semantics/altIdentifier/doi/10.1021/ie040021s
info:eu-repo/semantics/altIdentifier/url/https://pubs.acs.org/doi/10.1021/ie040021s
dc.rights.none.fl_str_mv info:eu-repo/semantics/openAccess
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
eu_rights_str_mv openAccess
rights_invalid_str_mv https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.format.none.fl_str_mv application/pdf
application/pdf
dc.publisher.none.fl_str_mv American Chemical Society
publisher.none.fl_str_mv American Chemical Society
dc.source.none.fl_str_mv reponame:CONICET Digital (CONICET)
instname:Consejo Nacional de Investigaciones Científicas y Técnicas
reponame_str CONICET Digital (CONICET)
collection CONICET Digital (CONICET)
instname_str Consejo Nacional de Investigaciones Científicas y Técnicas
repository.name.fl_str_mv CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicas
repository.mail.fl_str_mv dasensio@conicet.gov.ar; lcarlino@conicet.gov.ar
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score 12.982451

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