Optimal structure of reactive and non-reactive stages in reactive distillation processes

Autores
Domancich, Alejandro Omar; Brignole, Nélida Beatriz; Hoch, Patricia Monica
Año de publicación
2007
Idioma
inglés
Tipo de recurso
parte de libro
Estado
versión publicada
Descripción
We present a model for a reactive column, based on models by Taylor and Krishna (2000) and Almeida-Rivera (2005), shown in detail in Domancich et al (2006). It consists in pure separation stages combined with a reactive distillation sector, where both reaction and separation take place at the same time. For this study, we used a rigorous modeling of the column, with an equilibrium model for the reactive sector. An example showing the performance of a reactive distillation unit used for the production of MTBE is presented. The economic optimization of the reactive distillation process is performed using a MINLP algorithm and the cost of the resulting scheme is compared to the cost of the conventional process considering that reaction and separation take place in different equipment.
Fil: Domancich, Alejandro Omar. 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. Universidad Nacional del Sur. Departamento de Ciencias e Ingeniería de la Computación. Laboratorio de Ciencias de la Imágenes; Argentina
Fil: Brignole, Nélida Beatriz. 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. Universidad Nacional del Sur. Departamento de Ciencias e Ingeniería de la Computación. Laboratorio de Ciencias de la Imágenes; Argentina
Fil: Hoch, Patricia Monica. 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. Universidad Nacional del Sur. Departamento de Ingeniería Química; Argentina
Materia
REACTIVE COLUMN
DISTILLATION
MINLP
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:11336/133467
Acceder
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network_acronym_str CONICETDig
repository_id_str 3498
network_name_str CONICET Digital (CONICET)
spelling Optimal structure of reactive and non-reactive stages in reactive distillation processesDomancich, Alejandro OmarBrignole, Nélida BeatrizHoch, Patricia MonicaREACTIVE COLUMNDISTILLATIONMINLPhttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2We present a model for a reactive column, based on models by Taylor and Krishna (2000) and Almeida-Rivera (2005), shown in detail in Domancich et al (2006). It consists in pure separation stages combined with a reactive distillation sector, where both reaction and separation take place at the same time. For this study, we used a rigorous modeling of the column, with an equilibrium model for the reactive sector. An example showing the performance of a reactive distillation unit used for the production of MTBE is presented. The economic optimization of the reactive distillation process is performed using a MINLP algorithm and the cost of the resulting scheme is compared to the cost of the conventional process considering that reaction and separation take place in different equipment.Fil: Domancich, Alejandro Omar. 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. Universidad Nacional del Sur. Departamento de Ciencias e Ingeniería de la Computación. Laboratorio de Ciencias de la Imágenes; ArgentinaFil: Brignole, Nélida Beatriz. 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. Universidad Nacional del Sur. Departamento de Ciencias e Ingeniería de la Computación. Laboratorio de Ciencias de la Imágenes; ArgentinaFil: Hoch, Patricia Monica. 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. Universidad Nacional del Sur. Departamento de Ingeniería Química; ArgentinaItalian Association of Chemical EngineeringKlemeš, Jiří J.2007info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/bookParthttp://purl.org/coar/resource_type/c_3248info:ar-repo/semantics/parteDeLibroapplication/pdfapplication/pdfapplication/pdfapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/133467Domancich, Alejandro Omar; Brignole, Nélida Beatriz; Hoch, Patricia Monica; Optimal structure of reactive and non-reactive stages in reactive distillation processes; Italian Association of Chemical Engineering; XII; 2007; 85-9088-901915-4-62283-9216CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/url/https://www.aidic.it/cet/07/12/014.pdfinfo:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-09-10T13:01:05Zoai:ri.conicet.gov.ar:11336/133467instacron: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:34982025-09-10 13:01:05.212CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse
dc.title.none.fl_str_mv Optimal structure of reactive and non-reactive stages in reactive distillation processes
title Optimal structure of reactive and non-reactive stages in reactive distillation processes
spellingShingle Optimal structure of reactive and non-reactive stages in reactive distillation processes
Domancich, Alejandro Omar
REACTIVE COLUMN
DISTILLATION
MINLP
title_short Optimal structure of reactive and non-reactive stages in reactive distillation processes
title_full Optimal structure of reactive and non-reactive stages in reactive distillation processes
title_fullStr Optimal structure of reactive and non-reactive stages in reactive distillation processes
title_full_unstemmed Optimal structure of reactive and non-reactive stages in reactive distillation processes
title_sort Optimal structure of reactive and non-reactive stages in reactive distillation processes
dc.creator.none.fl_str_mv Domancich, Alejandro Omar
Brignole, Nélida Beatriz
Hoch, Patricia Monica
author Domancich, Alejandro Omar
author_facet Domancich, Alejandro Omar
Brignole, Nélida Beatriz
Hoch, Patricia Monica
author_role author
author2 Brignole, Nélida Beatriz
Hoch, Patricia Monica
author2_role author
author
dc.contributor.none.fl_str_mv Klemeš, Jiří J.
dc.subject.none.fl_str_mv REACTIVE COLUMN
DISTILLATION
MINLP
topic REACTIVE COLUMN
DISTILLATION
MINLP
purl_subject.fl_str_mv https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
dc.description.none.fl_txt_mv We present a model for a reactive column, based on models by Taylor and Krishna (2000) and Almeida-Rivera (2005), shown in detail in Domancich et al (2006). It consists in pure separation stages combined with a reactive distillation sector, where both reaction and separation take place at the same time. For this study, we used a rigorous modeling of the column, with an equilibrium model for the reactive sector. An example showing the performance of a reactive distillation unit used for the production of MTBE is presented. The economic optimization of the reactive distillation process is performed using a MINLP algorithm and the cost of the resulting scheme is compared to the cost of the conventional process considering that reaction and separation take place in different equipment.
Fil: Domancich, Alejandro Omar. 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. Universidad Nacional del Sur. Departamento de Ciencias e Ingeniería de la Computación. Laboratorio de Ciencias de la Imágenes; Argentina
Fil: Brignole, Nélida Beatriz. 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. Universidad Nacional del Sur. Departamento de Ciencias e Ingeniería de la Computación. Laboratorio de Ciencias de la Imágenes; Argentina
Fil: Hoch, Patricia Monica. 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. Universidad Nacional del Sur. Departamento de Ingeniería Química; Argentina
description We present a model for a reactive column, based on models by Taylor and Krishna (2000) and Almeida-Rivera (2005), shown in detail in Domancich et al (2006). It consists in pure separation stages combined with a reactive distillation sector, where both reaction and separation take place at the same time. For this study, we used a rigorous modeling of the column, with an equilibrium model for the reactive sector. An example showing the performance of a reactive distillation unit used for the production of MTBE is presented. The economic optimization of the reactive distillation process is performed using a MINLP algorithm and the cost of the resulting scheme is compared to the cost of the conventional process considering that reaction and separation take place in different equipment.
publishDate 2007
dc.date.none.fl_str_mv 2007
dc.type.none.fl_str_mv info:eu-repo/semantics/publishedVersion
info:eu-repo/semantics/bookPart
http://purl.org/coar/resource_type/c_3248
info:ar-repo/semantics/parteDeLibro
status_str publishedVersion
format bookPart
dc.identifier.none.fl_str_mv http://hdl.handle.net/11336/133467
Domancich, Alejandro Omar; Brignole, Nélida Beatriz; Hoch, Patricia Monica; Optimal structure of reactive and non-reactive stages in reactive distillation processes; Italian Association of Chemical Engineering; XII; 2007; 85-90
88-901915-4-6
2283-9216
CONICET Digital
CONICET
url http://hdl.handle.net/11336/133467
identifier_str_mv Domancich, Alejandro Omar; Brignole, Nélida Beatriz; Hoch, Patricia Monica; Optimal structure of reactive and non-reactive stages in reactive distillation processes; Italian Association of Chemical Engineering; XII; 2007; 85-90
88-901915-4-6
2283-9216
CONICET Digital
CONICET
dc.language.none.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv info:eu-repo/semantics/altIdentifier/url/https://www.aidic.it/cet/07/12/014.pdf
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
application/pdf
application/pdf
application/pdf
dc.publisher.none.fl_str_mv Italian Association of Chemical Engineering
publisher.none.fl_str_mv Italian Association of Chemical Engineering
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
_version_ 1842979924736999424
score 12.48226

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