Influence of tangent pinch points on the energy demand of batch distillations: Development of a conceptual model for binary mixtures
- Autores
- Torres, Karina Andrea; Espinosa, Hector Jose Maria
- Año de publicación
- 2011
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- This contribution explores the influence of tangent pinch points on the performance of batch distillations of highly nonideal binary mixtures and its incorporation into a conceptual modeling framework under the assumption of a rectifier with an infinite number of stages. First of all, the y−x diagram is divided into three regions taking into account both the inflection point (IP) in the phase diagram and the slope of the equilibrium curve at xD = 1. After that, limiting values for the reflux ratio and distillate composition; namely, r* and xD*, are calculated for the instantaneous still composition xB with the aid of region-dependent algorithms, which incorporate the tangency condition in different ways. Finally, the instantaneous column performance is estimated taking into account the selected operation mode; i.e., constant reflux ratio or constant distillate composition. Applied to the mixture acetone−water, results for complete simulations are presented in terms of both rectification advance and operation time. A brief comparative study on the minimum energy demand required for a given separation as estimated from models with and without tangent pinches is also carried out.
Fil: Torres, Karina Andrea. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo y Diseño. Universidad Tecnológica Nacional. Facultad Regional Santa Fe. Instituto de Desarrollo y Diseño; Argentina
Fil: Espinosa, Hector Jose Maria. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo y Diseño. Universidad Tecnológica Nacional. Facultad Regional Santa Fe. Instituto de Desarrollo y Diseño; Argentina - Materia
-
PINCH
ENERGY
DEMAND
BATCH - 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:11336/137169
Ver los metadatos del registro completo
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Influence of tangent pinch points on the energy demand of batch distillations: Development of a conceptual model for binary mixturesTorres, Karina AndreaEspinosa, Hector Jose MariaPINCHENERGYDEMANDBATCHhttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2This contribution explores the influence of tangent pinch points on the performance of batch distillations of highly nonideal binary mixtures and its incorporation into a conceptual modeling framework under the assumption of a rectifier with an infinite number of stages. First of all, the y−x diagram is divided into three regions taking into account both the inflection point (IP) in the phase diagram and the slope of the equilibrium curve at xD = 1. After that, limiting values for the reflux ratio and distillate composition; namely, r* and xD*, are calculated for the instantaneous still composition xB with the aid of region-dependent algorithms, which incorporate the tangency condition in different ways. Finally, the instantaneous column performance is estimated taking into account the selected operation mode; i.e., constant reflux ratio or constant distillate composition. Applied to the mixture acetone−water, results for complete simulations are presented in terms of both rectification advance and operation time. A brief comparative study on the minimum energy demand required for a given separation as estimated from models with and without tangent pinches is also carried out.Fil: Torres, Karina Andrea. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo y Diseño. Universidad Tecnológica Nacional. Facultad Regional Santa Fe. Instituto de Desarrollo y Diseño; ArgentinaFil: Espinosa, Hector Jose Maria. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo y Diseño. Universidad Tecnológica Nacional. Facultad Regional Santa Fe. Instituto de Desarrollo y Diseño; ArgentinaAmerican Chemical Society2011-04-08info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/137169Torres, Karina Andrea; Espinosa, Hector Jose Maria; Influence of tangent pinch points on the energy demand of batch distillations: Development of a conceptual model for binary mixtures; American Chemical Society; Industrial & Engineering Chemical Research; 50; 10; 8-4-2011; 6260-62750888-5885CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/url/https://pubs.acs.org/doi/10.1021/ie101894qinfo:eu-repo/semantics/altIdentifier/doi/10.1021/ie101894qinfo:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-10-22T11:13:12Zoai:ri.conicet.gov.ar:11336/137169instacron: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 11:13:13.126CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
| dc.title.none.fl_str_mv |
Influence of tangent pinch points on the energy demand of batch distillations: Development of a conceptual model for binary mixtures |
| title |
Influence of tangent pinch points on the energy demand of batch distillations: Development of a conceptual model for binary mixtures |
| spellingShingle |
Influence of tangent pinch points on the energy demand of batch distillations: Development of a conceptual model for binary mixtures Torres, Karina Andrea PINCH ENERGY DEMAND BATCH |
| title_short |
Influence of tangent pinch points on the energy demand of batch distillations: Development of a conceptual model for binary mixtures |
| title_full |
Influence of tangent pinch points on the energy demand of batch distillations: Development of a conceptual model for binary mixtures |
| title_fullStr |
Influence of tangent pinch points on the energy demand of batch distillations: Development of a conceptual model for binary mixtures |
| title_full_unstemmed |
Influence of tangent pinch points on the energy demand of batch distillations: Development of a conceptual model for binary mixtures |
| title_sort |
Influence of tangent pinch points on the energy demand of batch distillations: Development of a conceptual model for binary mixtures |
| dc.creator.none.fl_str_mv |
Torres, Karina Andrea Espinosa, Hector Jose Maria |
| author |
Torres, Karina Andrea |
| author_facet |
Torres, Karina Andrea Espinosa, Hector Jose Maria |
| author_role |
author |
| author2 |
Espinosa, Hector Jose Maria |
| author2_role |
author |
| dc.subject.none.fl_str_mv |
PINCH ENERGY DEMAND BATCH |
| topic |
PINCH ENERGY DEMAND BATCH |
| purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2.4 https://purl.org/becyt/ford/2 |
| dc.description.none.fl_txt_mv |
This contribution explores the influence of tangent pinch points on the performance of batch distillations of highly nonideal binary mixtures and its incorporation into a conceptual modeling framework under the assumption of a rectifier with an infinite number of stages. First of all, the y−x diagram is divided into three regions taking into account both the inflection point (IP) in the phase diagram and the slope of the equilibrium curve at xD = 1. After that, limiting values for the reflux ratio and distillate composition; namely, r* and xD*, are calculated for the instantaneous still composition xB with the aid of region-dependent algorithms, which incorporate the tangency condition in different ways. Finally, the instantaneous column performance is estimated taking into account the selected operation mode; i.e., constant reflux ratio or constant distillate composition. Applied to the mixture acetone−water, results for complete simulations are presented in terms of both rectification advance and operation time. A brief comparative study on the minimum energy demand required for a given separation as estimated from models with and without tangent pinches is also carried out. Fil: Torres, Karina Andrea. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo y Diseño. Universidad Tecnológica Nacional. Facultad Regional Santa Fe. Instituto de Desarrollo y Diseño; Argentina Fil: Espinosa, Hector Jose Maria. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo y Diseño. Universidad Tecnológica Nacional. Facultad Regional Santa Fe. Instituto de Desarrollo y Diseño; Argentina |
| description |
This contribution explores the influence of tangent pinch points on the performance of batch distillations of highly nonideal binary mixtures and its incorporation into a conceptual modeling framework under the assumption of a rectifier with an infinite number of stages. First of all, the y−x diagram is divided into three regions taking into account both the inflection point (IP) in the phase diagram and the slope of the equilibrium curve at xD = 1. After that, limiting values for the reflux ratio and distillate composition; namely, r* and xD*, are calculated for the instantaneous still composition xB with the aid of region-dependent algorithms, which incorporate the tangency condition in different ways. Finally, the instantaneous column performance is estimated taking into account the selected operation mode; i.e., constant reflux ratio or constant distillate composition. Applied to the mixture acetone−water, results for complete simulations are presented in terms of both rectification advance and operation time. A brief comparative study on the minimum energy demand required for a given separation as estimated from models with and without tangent pinches is also carried out. |
| publishDate |
2011 |
| dc.date.none.fl_str_mv |
2011-04-08 |
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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/11336/137169 Torres, Karina Andrea; Espinosa, Hector Jose Maria; Influence of tangent pinch points on the energy demand of batch distillations: Development of a conceptual model for binary mixtures; American Chemical Society; Industrial & Engineering Chemical Research; 50; 10; 8-4-2011; 6260-6275 0888-5885 CONICET Digital CONICET |
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http://hdl.handle.net/11336/137169 |
| identifier_str_mv |
Torres, Karina Andrea; Espinosa, Hector Jose Maria; Influence of tangent pinch points on the energy demand of batch distillations: Development of a conceptual model for binary mixtures; American Chemical Society; Industrial & Engineering Chemical Research; 50; 10; 8-4-2011; 6260-6275 0888-5885 CONICET Digital CONICET |
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eng |
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eng |
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American Chemical Society |
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American Chemical Society |
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