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
.jpg)
- Institución
- Consejo Nacional de Investigaciones Científicas y Técnicas
- OAI Identificador
- oai:ri.conicet.gov.ar:11336/20479
Ver los metadatos del registro completo
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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 Técnicas2025-11-26T08:56:00Zoai: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:34982025-11-26 08:56:00.665CONICET 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 |
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2009-12 |
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info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion http://purl.org/coar/resource_type/c_6501 info:ar-repo/semantics/articulo |
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article |
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publishedVersion |
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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 |
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http://hdl.handle.net/11336/20479 |
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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 |
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eng |
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eng |
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Planta Piloto de Ingeniería Química |
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