Design of optimal reactive distillation processes for etbe production using rigorous thermodynamic models
- Autores
- Durruty, Gisela Noel; Diaz, Maria Soledad; Hoch, Patricia Monica
- Año de publicación
- 2014
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- In this work we propose a model for the design of a reactive distillation unit for ETBE synthesis from ethanol and isobutene, with both rigorous thermodynamic models (UNIFAC and SRK) and hydraulic constraints, in an equation oriented environment within GAMS. The objective is to minimize total annual cost. The main contribution of this paper is the estimation of binary interaction parameters yet unavailable for the system being considered, using experimental data taken from literature, within a reactive distillation column optimization environment.
Fil: Durruty, Gisela Noel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Bahía Blanca. Planta Piloto de Ingeniería Química (i); Argentina. Universidad Nacional del Sur. Departamento de Ingenieria Quimica; Argentina
Fil: Diaz, Maria Soledad. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Bahía Blanca. Planta Piloto de Ingeniería Química (i); Argentina. Universidad Nacional del Sur. Departamento de Ingenieria Quimica; Argentina
Fil: Hoch, Patricia Monica. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Bahía Blanca. Planta Piloto de Ingeniería Química (i); Argentina. Universidad Nacional del Sur. Departamento de Ingenieria Quimica; Argentina - Materia
-
Reactive Distillation
Process Intensification
Thermodynamics - Nivel de accesibilidad
- acceso abierto
- Condiciones de uso
- https://creativecommons.org/licenses/by-nc-nd/2.5/ar/
- Repositorio
- Institución
- Consejo Nacional de Investigaciones Científicas y Técnicas
- OAI Identificador
- oai:ri.conicet.gov.ar:11336/13543
Ver los metadatos del registro completo
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Design of optimal reactive distillation processes for etbe production using rigorous thermodynamic modelsDurruty, Gisela NoelDiaz, Maria SoledadHoch, Patricia MonicaReactive DistillationProcess IntensificationThermodynamicshttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2In this work we propose a model for the design of a reactive distillation unit for ETBE synthesis from ethanol and isobutene, with both rigorous thermodynamic models (UNIFAC and SRK) and hydraulic constraints, in an equation oriented environment within GAMS. The objective is to minimize total annual cost. The main contribution of this paper is the estimation of binary interaction parameters yet unavailable for the system being considered, using experimental data taken from literature, within a reactive distillation column optimization environment.Fil: Durruty, Gisela Noel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Bahía Blanca. Planta Piloto de Ingeniería Química (i); Argentina. Universidad Nacional del Sur. Departamento de Ingenieria Quimica; ArgentinaFil: Diaz, Maria Soledad. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Bahía Blanca. Planta Piloto de Ingeniería Química (i); Argentina. Universidad Nacional del Sur. Departamento de Ingenieria Quimica; ArgentinaFil: Hoch, Patricia Monica. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Bahía Blanca. Planta Piloto de Ingeniería Química (i); Argentina. Universidad Nacional del Sur. Departamento de Ingenieria Quimica; ArgentinaElsevier Science2014info: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/11336/13543Durruty, Gisela Noel; Diaz, Maria Soledad; Hoch, Patricia Monica; Design of optimal reactive distillation processes for etbe production using rigorous thermodynamic models; Elsevier Science; Computer Aided Chemical Engineering; 33; -1-2014; 1591-15961570-7946enginfo:eu-repo/semantics/altIdentifier/url/http://www.sciencedirect.com/science/article/pii/B9780444634559501008info:eu-repo/semantics/altIdentifier/doi/10.1016/B978-0-444-63455-9.50100-8info:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-nd/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-10-15T15:21:27Zoai:ri.conicet.gov.ar:11336/13543instacron: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:34982025-10-15 15:21:28.14CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
dc.title.none.fl_str_mv |
Design of optimal reactive distillation processes for etbe production using rigorous thermodynamic models |
title |
Design of optimal reactive distillation processes for etbe production using rigorous thermodynamic models |
spellingShingle |
Design of optimal reactive distillation processes for etbe production using rigorous thermodynamic models Durruty, Gisela Noel Reactive Distillation Process Intensification Thermodynamics |
title_short |
Design of optimal reactive distillation processes for etbe production using rigorous thermodynamic models |
title_full |
Design of optimal reactive distillation processes for etbe production using rigorous thermodynamic models |
title_fullStr |
Design of optimal reactive distillation processes for etbe production using rigorous thermodynamic models |
title_full_unstemmed |
Design of optimal reactive distillation processes for etbe production using rigorous thermodynamic models |
title_sort |
Design of optimal reactive distillation processes for etbe production using rigorous thermodynamic models |
dc.creator.none.fl_str_mv |
Durruty, Gisela Noel Diaz, Maria Soledad Hoch, Patricia Monica |
author |
Durruty, Gisela Noel |
author_facet |
Durruty, Gisela Noel Diaz, Maria Soledad Hoch, Patricia Monica |
author_role |
author |
author2 |
Diaz, Maria Soledad Hoch, Patricia Monica |
author2_role |
author author |
dc.subject.none.fl_str_mv |
Reactive Distillation Process Intensification Thermodynamics |
topic |
Reactive Distillation Process Intensification Thermodynamics |
purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2.4 https://purl.org/becyt/ford/2 |
dc.description.none.fl_txt_mv |
In this work we propose a model for the design of a reactive distillation unit for ETBE synthesis from ethanol and isobutene, with both rigorous thermodynamic models (UNIFAC and SRK) and hydraulic constraints, in an equation oriented environment within GAMS. The objective is to minimize total annual cost. The main contribution of this paper is the estimation of binary interaction parameters yet unavailable for the system being considered, using experimental data taken from literature, within a reactive distillation column optimization environment. Fil: Durruty, Gisela Noel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Bahía Blanca. Planta Piloto de Ingeniería Química (i); Argentina. Universidad Nacional del Sur. Departamento de Ingenieria Quimica; Argentina Fil: Diaz, Maria Soledad. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Bahía Blanca. Planta Piloto de Ingeniería Química (i); Argentina. Universidad Nacional del Sur. Departamento de Ingenieria Quimica; Argentina Fil: Hoch, Patricia Monica. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Bahía Blanca. Planta Piloto de Ingeniería Química (i); Argentina. Universidad Nacional del Sur. Departamento de Ingenieria Quimica; Argentina |
description |
In this work we propose a model for the design of a reactive distillation unit for ETBE synthesis from ethanol and isobutene, with both rigorous thermodynamic models (UNIFAC and SRK) and hydraulic constraints, in an equation oriented environment within GAMS. The objective is to minimize total annual cost. The main contribution of this paper is the estimation of binary interaction parameters yet unavailable for the system being considered, using experimental data taken from literature, within a reactive distillation column optimization environment. |
publishDate |
2014 |
dc.date.none.fl_str_mv |
2014 |
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/11336/13543 Durruty, Gisela Noel; Diaz, Maria Soledad; Hoch, Patricia Monica; Design of optimal reactive distillation processes for etbe production using rigorous thermodynamic models; Elsevier Science; Computer Aided Chemical Engineering; 33; -1-2014; 1591-1596 1570-7946 |
url |
http://hdl.handle.net/11336/13543 |
identifier_str_mv |
Durruty, Gisela Noel; Diaz, Maria Soledad; Hoch, Patricia Monica; Design of optimal reactive distillation processes for etbe production using rigorous thermodynamic models; Elsevier Science; Computer Aided Chemical Engineering; 33; -1-2014; 1591-1596 1570-7946 |
dc.language.none.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
info:eu-repo/semantics/altIdentifier/url/http://www.sciencedirect.com/science/article/pii/B9780444634559501008 info:eu-repo/semantics/altIdentifier/doi/10.1016/B978-0-444-63455-9.50100-8 |
dc.rights.none.fl_str_mv |
info:eu-repo/semantics/openAccess https://creativecommons.org/licenses/by-nc-nd/2.5/ar/ |
eu_rights_str_mv |
openAccess |
rights_invalid_str_mv |
https://creativecommons.org/licenses/by-nc-nd/2.5/ar/ |
dc.format.none.fl_str_mv |
application/pdf application/pdf application/pdf |
dc.publisher.none.fl_str_mv |
Elsevier Science |
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Elsevier Science |
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CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicas |
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