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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| 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 Técnicas2025-10-29T12:11:29Zoai: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:34982025-10-29 12:11:29.933CONICET 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 | 
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| 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 | 
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