Effect of Vapor-Liquid Equilibrium Data on the Design of Separation Sequences by Distillation

Autores
Parodi, C. A.; Campanella, Enrique Angel
Año de publicación
2009
Idioma
inglés
Tipo de recurso
artículo
Estado
versión publicada
Descripción
An evaluation of the effect of vapor-liquid equilibrium experimental data on the design of separation sequences by distillation was done using computer simulation. Separation of a mixture of ace-tone-chloroform-benzene was chosen as an example problem. Two sequences were compared. To quantify the thermodynamic data uncertainties for each se-quence two sets of binary vapor-liquid equilibrium data were chosen. These two sets of data were used to generate simulation cases as in classical two-level fac-torial design of experiments. A third set of binary va-por-liquid experimental data allows comparing phase liquid models. For the two-column sequence, analysis done to each column alone or to the whole sequence gave the same results. In the three-column sequence, results were different and simulation of the whole se-quence gave a complete different account that simula-tion of each column alone.
Fil: Parodi, C. A.. Universidad Nacional del Litoral; Argentina
Fil: Campanella, Enrique Angel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo Tecnológico para la Industria Química. Universidad Nacional del Litoral. Instituto de Desarrollo Tecnológico para la Industria Química; Argentina
Materia
Azeotropic Distillation
Sensitivity Analysis
Phase Equilibrium
Azeotrope
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:11336/20479

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spelling Effect of Vapor-Liquid Equilibrium Data on the Design of Separation Sequences by DistillationParodi, C. A.Campanella, Enrique AngelAzeotropic DistillationSensitivity AnalysisPhase EquilibriumAzeotropehttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2An evaluation of the effect of vapor-liquid equilibrium experimental data on the design of separation sequences by distillation was done using computer simulation. Separation of a mixture of ace-tone-chloroform-benzene was chosen as an example problem. Two sequences were compared. To quantify the thermodynamic data uncertainties for each se-quence two sets of binary vapor-liquid equilibrium data were chosen. These two sets of data were used to generate simulation cases as in classical two-level fac-torial design of experiments. A third set of binary va-por-liquid experimental data allows comparing phase liquid models. For the two-column sequence, analysis done to each column alone or to the whole sequence gave the same results. In the three-column sequence, results were different and simulation of the whole se-quence gave a complete different account that simula-tion of each column alone.Fil: Parodi, C. A.. Universidad Nacional del Litoral; ArgentinaFil: Campanella, Enrique Angel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo Tecnológico para la Industria Química. Universidad Nacional del Litoral. Instituto de Desarrollo Tecnológico para la Industria Química; ArgentinaPlanta Piloto de Ingeniería Química2009-12info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/20479Parodi, C. A.; Campanella, Enrique Angel; Effect of Vapor-Liquid Equilibrium Data on the Design of Separation Sequences by Distillation; Planta Piloto de Ingeniería Química; Latin American Applied Research; 39; 1; 12-2009; 33-400327-07931851-8796CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/url/http://www.laar.uns.edu.ar/indexes/artic_v3901/Vol_39_1_p33.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 Técnicas2025-09-10T13:14:09Zoai:ri.conicet.gov.ar:11336/20479instacron: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 13:14:09.41CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse
dc.title.none.fl_str_mv Effect of Vapor-Liquid Equilibrium Data on the Design of Separation Sequences by Distillation
title Effect of Vapor-Liquid Equilibrium Data on the Design of Separation Sequences by Distillation
spellingShingle Effect of Vapor-Liquid Equilibrium Data on the Design of Separation Sequences by Distillation
Parodi, C. A.
Azeotropic Distillation
Sensitivity Analysis
Phase Equilibrium
Azeotrope
title_short Effect of Vapor-Liquid Equilibrium Data on the Design of Separation Sequences by Distillation
title_full Effect of Vapor-Liquid Equilibrium Data on the Design of Separation Sequences by Distillation
title_fullStr Effect of Vapor-Liquid Equilibrium Data on the Design of Separation Sequences by Distillation
title_full_unstemmed Effect of Vapor-Liquid Equilibrium Data on the Design of Separation Sequences by Distillation
title_sort Effect of Vapor-Liquid Equilibrium Data on the Design of Separation Sequences by Distillation
dc.creator.none.fl_str_mv Parodi, C. A.
Campanella, Enrique Angel
author Parodi, C. A.
author_facet Parodi, C. A.
Campanella, Enrique Angel
author_role author
author2 Campanella, Enrique Angel
author2_role author
dc.subject.none.fl_str_mv Azeotropic Distillation
Sensitivity Analysis
Phase Equilibrium
Azeotrope
topic Azeotropic Distillation
Sensitivity Analysis
Phase Equilibrium
Azeotrope
purl_subject.fl_str_mv https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
dc.description.none.fl_txt_mv An evaluation of the effect of vapor-liquid equilibrium experimental data on the design of separation sequences by distillation was done using computer simulation. Separation of a mixture of ace-tone-chloroform-benzene was chosen as an example problem. Two sequences were compared. To quantify the thermodynamic data uncertainties for each se-quence two sets of binary vapor-liquid equilibrium data were chosen. These two sets of data were used to generate simulation cases as in classical two-level fac-torial design of experiments. A third set of binary va-por-liquid experimental data allows comparing phase liquid models. For the two-column sequence, analysis done to each column alone or to the whole sequence gave the same results. In the three-column sequence, results were different and simulation of the whole se-quence gave a complete different account that simula-tion of each column alone.
Fil: Parodi, C. A.. Universidad Nacional del Litoral; Argentina
Fil: Campanella, Enrique Angel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo Tecnológico para la Industria Química. Universidad Nacional del Litoral. Instituto de Desarrollo Tecnológico para la Industria Química; Argentina
description An evaluation of the effect of vapor-liquid equilibrium experimental data on the design of separation sequences by distillation was done using computer simulation. Separation of a mixture of ace-tone-chloroform-benzene was chosen as an example problem. Two sequences were compared. To quantify the thermodynamic data uncertainties for each se-quence two sets of binary vapor-liquid equilibrium data were chosen. These two sets of data were used to generate simulation cases as in classical two-level fac-torial design of experiments. A third set of binary va-por-liquid experimental data allows comparing phase liquid models. For the two-column sequence, analysis done to each column alone or to the whole sequence gave the same results. In the three-column sequence, results were different and simulation of the whole se-quence gave a complete different account that simula-tion of each column alone.
publishDate 2009
dc.date.none.fl_str_mv 2009-12
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/11336/20479
Parodi, C. A.; Campanella, Enrique Angel; Effect of Vapor-Liquid Equilibrium Data on the Design of Separation Sequences by Distillation; Planta Piloto de Ingeniería Química; Latin American Applied Research; 39; 1; 12-2009; 33-40
0327-0793
1851-8796
CONICET Digital
CONICET
url http://hdl.handle.net/11336/20479
identifier_str_mv Parodi, C. A.; Campanella, Enrique Angel; Effect of Vapor-Liquid Equilibrium Data on the Design of Separation Sequences by Distillation; Planta Piloto de Ingeniería Química; Latin American Applied Research; 39; 1; 12-2009; 33-40
0327-0793
1851-8796
CONICET Digital
CONICET
dc.language.none.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv info:eu-repo/semantics/altIdentifier/url/http://www.laar.uns.edu.ar/indexes/artic_v3901/Vol_39_1_p33.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
dc.publisher.none.fl_str_mv Planta Piloto de Ingeniería Química
publisher.none.fl_str_mv Planta Piloto de Ingeniería Química
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 12.993085