Optimization of the operating conditions of azeotropic distillation columns with pervaporation membranes
- Autores
- Hoch, Patricia Monica; Daviou, Maria Carolina; Eliceche, Ana Maria
- Año de publicación
- 2003
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- The main objective of this work is the optimization of the operating conditions of azeotropic distillation columns in hybrid distillation/pervaporation systems. In the configuration analyzed, a liquid side stream extracted from the azeotropic distillation column with the distributing non-key component is treated in a pervaporation membrane while the retentate is recycled to the column. The pervaporation membrane separates the pure distributing non-key component from the mixture, thus helping to improve the purity in the top and/or bottom products of the distillation column. The case study shows the hybrid process of a distillation column combined with pervaporation membranes, compared to the classical two-column process for Methyl tert-Butyl Ether production. In both cases, the operating conditions of the distillation columns such as reflux ratio, product and side draw flowrates are selected optimally. The numerical results show a significant reduction in operating cost obtained by using a pervaporation membrane instead of the second column in the original process.
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
Fil: Daviou, Maria Carolina. 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
Fil: Eliceche, Ana Maria. 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 - Materia
-
Azeotropic
Distillation
Pervaporation
membranes - 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:11336/101429
Ver los metadatos del registro completo
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Optimization of the operating conditions of azeotropic distillation columns with pervaporation membranesHoch, Patricia MonicaDaviou, Maria CarolinaEliceche, Ana MariaAzeotropicDistillationPervaporationmembraneshttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2The main objective of this work is the optimization of the operating conditions of azeotropic distillation columns in hybrid distillation/pervaporation systems. In the configuration analyzed, a liquid side stream extracted from the azeotropic distillation column with the distributing non-key component is treated in a pervaporation membrane while the retentate is recycled to the column. The pervaporation membrane separates the pure distributing non-key component from the mixture, thus helping to improve the purity in the top and/or bottom products of the distillation column. The case study shows the hybrid process of a distillation column combined with pervaporation membranes, compared to the classical two-column process for Methyl tert-Butyl Ether production. In both cases, the operating conditions of the distillation columns such as reflux ratio, product and side draw flowrates are selected optimally. The numerical results show a significant reduction in operating cost obtained by using a pervaporation membrane instead of the second column in the original process.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; ArgentinaFil: Daviou, Maria Carolina. 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; ArgentinaFil: Eliceche, Ana Maria. 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; ArgentinaPlanta Piloto de Ingeniería Química2003-06info: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/11336/101429Hoch, Patricia Monica; Daviou, Maria Carolina; Eliceche, Ana Maria; Optimization of the operating conditions of azeotropic distillation columns with pervaporation membranes; Planta Piloto de Ingeniería Química; Latin American Applied Research; 33; 2; 6-2003; 177-1830327-07931851-8796CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/url/http://www.oalib.com/paper/2135907#.XoJfUohKjIUinfo:eu-repo/semantics/altIdentifier/url/http://www.scielo.org.ar/scielo.php?script=sci_arttext&pid=S0327-07932003000200018info:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-11-05T10:48:47Zoai:ri.conicet.gov.ar:11336/101429instacron: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:34982025-11-05 10:48:47.7CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
| dc.title.none.fl_str_mv |
Optimization of the operating conditions of azeotropic distillation columns with pervaporation membranes |
| title |
Optimization of the operating conditions of azeotropic distillation columns with pervaporation membranes |
| spellingShingle |
Optimization of the operating conditions of azeotropic distillation columns with pervaporation membranes Hoch, Patricia Monica Azeotropic Distillation Pervaporation membranes |
| title_short |
Optimization of the operating conditions of azeotropic distillation columns with pervaporation membranes |
| title_full |
Optimization of the operating conditions of azeotropic distillation columns with pervaporation membranes |
| title_fullStr |
Optimization of the operating conditions of azeotropic distillation columns with pervaporation membranes |
| title_full_unstemmed |
Optimization of the operating conditions of azeotropic distillation columns with pervaporation membranes |
| title_sort |
Optimization of the operating conditions of azeotropic distillation columns with pervaporation membranes |
| dc.creator.none.fl_str_mv |
Hoch, Patricia Monica Daviou, Maria Carolina Eliceche, Ana Maria |
| author |
Hoch, Patricia Monica |
| author_facet |
Hoch, Patricia Monica Daviou, Maria Carolina Eliceche, Ana Maria |
| author_role |
author |
| author2 |
Daviou, Maria Carolina Eliceche, Ana Maria |
| author2_role |
author author |
| dc.subject.none.fl_str_mv |
Azeotropic Distillation Pervaporation membranes |
| topic |
Azeotropic Distillation Pervaporation membranes |
| purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2.4 https://purl.org/becyt/ford/2 |
| dc.description.none.fl_txt_mv |
The main objective of this work is the optimization of the operating conditions of azeotropic distillation columns in hybrid distillation/pervaporation systems. In the configuration analyzed, a liquid side stream extracted from the azeotropic distillation column with the distributing non-key component is treated in a pervaporation membrane while the retentate is recycled to the column. The pervaporation membrane separates the pure distributing non-key component from the mixture, thus helping to improve the purity in the top and/or bottom products of the distillation column. The case study shows the hybrid process of a distillation column combined with pervaporation membranes, compared to the classical two-column process for Methyl tert-Butyl Ether production. In both cases, the operating conditions of the distillation columns such as reflux ratio, product and side draw flowrates are selected optimally. The numerical results show a significant reduction in operating cost obtained by using a pervaporation membrane instead of the second column in the original process. 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 Fil: Daviou, Maria Carolina. 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 Fil: Eliceche, Ana Maria. 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 |
| description |
The main objective of this work is the optimization of the operating conditions of azeotropic distillation columns in hybrid distillation/pervaporation systems. In the configuration analyzed, a liquid side stream extracted from the azeotropic distillation column with the distributing non-key component is treated in a pervaporation membrane while the retentate is recycled to the column. The pervaporation membrane separates the pure distributing non-key component from the mixture, thus helping to improve the purity in the top and/or bottom products of the distillation column. The case study shows the hybrid process of a distillation column combined with pervaporation membranes, compared to the classical two-column process for Methyl tert-Butyl Ether production. In both cases, the operating conditions of the distillation columns such as reflux ratio, product and side draw flowrates are selected optimally. The numerical results show a significant reduction in operating cost obtained by using a pervaporation membrane instead of the second column in the original process. |
| publishDate |
2003 |
| dc.date.none.fl_str_mv |
2003-06 |
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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 |
| dc.identifier.none.fl_str_mv |
http://hdl.handle.net/11336/101429 Hoch, Patricia Monica; Daviou, Maria Carolina; Eliceche, Ana Maria; Optimization of the operating conditions of azeotropic distillation columns with pervaporation membranes; Planta Piloto de Ingeniería Química; Latin American Applied Research; 33; 2; 6-2003; 177-183 0327-0793 1851-8796 CONICET Digital CONICET |
| url |
http://hdl.handle.net/11336/101429 |
| identifier_str_mv |
Hoch, Patricia Monica; Daviou, Maria Carolina; Eliceche, Ana Maria; Optimization of the operating conditions of azeotropic distillation columns with pervaporation membranes; Planta Piloto de Ingeniería Química; Latin American Applied Research; 33; 2; 6-2003; 177-183 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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