Shortcut Procedure for Inverted Batch Distillation Column. I Multicomponent Ideal System

Autores
Xu, Sonling; Salomone, Hector Enrique; Iribarren, Oscar Alberto
Año de publicación
2001
Idioma
inglés
Tipo de recurso
artículo
Estado
versión publicada
Descripción
A model for batch stripping distillation is presented, equivalent to the Fenske - Underwood - Gillilang model for continuous distillation. Given a separation task, we propose to compute the minimun number of trays and reflux ratio to perform the separation by batch stripping distillation. Then, it is shown that the performance of real columns with a finite given number of trays N and reflux ratio R, can be represented by a Guilliland type correlation, as a function of the minimum values of N and R.
Fil: Xu, Sonling. Tianjing University; China
Fil: Salomone, Hector Enrique. 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: Iribarren, Oscar Alberto. 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
BATCH
DISTILLATION
STRIPPING
SHORTCUT
Nivel de accesibilidad
acceso abierto
Condiciones de uso
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
Repositorio
CONICET Digital (CONICET)
Institución
Consejo Nacional de Investigaciones Científicas y Técnicas
OAI Identificador
oai:ri.conicet.gov.ar:11336/99295
Acceder
id CONICETDig_d3a7a27c55ac38502799aafef1a04b0f
oai_identifier_str oai:ri.conicet.gov.ar:11336/99295
network_acronym_str CONICETDig
repository_id_str 3498
network_name_str CONICET Digital (CONICET)
spelling Shortcut Procedure for Inverted Batch Distillation Column. I Multicomponent Ideal SystemXu, SonlingSalomone, Hector EnriqueIribarren, Oscar AlbertoBATCHDISTILLATIONSTRIPPINGSHORTCUThttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2A model for batch stripping distillation is presented, equivalent to the Fenske - Underwood - Gillilang model for continuous distillation. Given a separation task, we propose to compute the minimun number of trays and reflux ratio to perform the separation by batch stripping distillation. Then, it is shown that the performance of real columns with a finite given number of trays N and reflux ratio R, can be represented by a Guilliland type correlation, as a function of the minimum values of N and R.Fil: Xu, Sonling. Tianjing University; ChinaFil: Salomone, Hector Enrique. 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: Iribarren, Oscar Alberto. 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; ArgentinaChemical Industry Press2001-01info: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/11336/99295Xu, Sonling; Salomone, Hector Enrique; Iribarren, Oscar Alberto; Shortcut Procedure for Inverted Batch Distillation Column. I Multicomponent Ideal System; Chemical Industry Press; Chinese Journal Of Chemical Engineering; 9; 1; 1-2001; 28-331004-9541CONICET DigitalCONICETenginfo:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-09-03T09:55:26Zoai:ri.conicet.gov.ar:11336/99295instacron: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:34982025-09-03 09:55:26.814CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse
dc.title.none.fl_str_mv Shortcut Procedure for Inverted Batch Distillation Column. I Multicomponent Ideal System
title Shortcut Procedure for Inverted Batch Distillation Column. I Multicomponent Ideal System
spellingShingle Shortcut Procedure for Inverted Batch Distillation Column. I Multicomponent Ideal System
Xu, Sonling
BATCH
DISTILLATION
STRIPPING
SHORTCUT
title_short Shortcut Procedure for Inverted Batch Distillation Column. I Multicomponent Ideal System
title_full Shortcut Procedure for Inverted Batch Distillation Column. I Multicomponent Ideal System
title_fullStr Shortcut Procedure for Inverted Batch Distillation Column. I Multicomponent Ideal System
title_full_unstemmed Shortcut Procedure for Inverted Batch Distillation Column. I Multicomponent Ideal System
title_sort Shortcut Procedure for Inverted Batch Distillation Column. I Multicomponent Ideal System
dc.creator.none.fl_str_mv Xu, Sonling
Salomone, Hector Enrique
Iribarren, Oscar Alberto
author Xu, Sonling
author_facet Xu, Sonling
Salomone, Hector Enrique
Iribarren, Oscar Alberto
author_role author
author2 Salomone, Hector Enrique
Iribarren, Oscar Alberto
author2_role author
author
dc.subject.none.fl_str_mv BATCH
DISTILLATION
STRIPPING
SHORTCUT
topic BATCH
DISTILLATION
STRIPPING
SHORTCUT
purl_subject.fl_str_mv https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
dc.description.none.fl_txt_mv A model for batch stripping distillation is presented, equivalent to the Fenske - Underwood - Gillilang model for continuous distillation. Given a separation task, we propose to compute the minimun number of trays and reflux ratio to perform the separation by batch stripping distillation. Then, it is shown that the performance of real columns with a finite given number of trays N and reflux ratio R, can be represented by a Guilliland type correlation, as a function of the minimum values of N and R.
Fil: Xu, Sonling. Tianjing University; China
Fil: Salomone, Hector Enrique. 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: Iribarren, Oscar Alberto. 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 A model for batch stripping distillation is presented, equivalent to the Fenske - Underwood - Gillilang model for continuous distillation. Given a separation task, we propose to compute the minimun number of trays and reflux ratio to perform the separation by batch stripping distillation. Then, it is shown that the performance of real columns with a finite given number of trays N and reflux ratio R, can be represented by a Guilliland type correlation, as a function of the minimum values of N and R.
publishDate 2001
dc.date.none.fl_str_mv 2001-01
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/11336/99295
Xu, Sonling; Salomone, Hector Enrique; Iribarren, Oscar Alberto; Shortcut Procedure for Inverted Batch Distillation Column. I Multicomponent Ideal System; Chemical Industry Press; Chinese Journal Of Chemical Engineering; 9; 1; 1-2001; 28-33
1004-9541
CONICET Digital
CONICET
url http://hdl.handle.net/11336/99295
identifier_str_mv Xu, Sonling; Salomone, Hector Enrique; Iribarren, Oscar Alberto; Shortcut Procedure for Inverted Batch Distillation Column. I Multicomponent Ideal System; Chemical Industry Press; Chinese Journal Of Chemical Engineering; 9; 1; 1-2001; 28-33
1004-9541
CONICET Digital
CONICET
dc.language.none.fl_str_mv eng
language eng
dc.rights.none.fl_str_mv info:eu-repo/semantics/openAccess
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
eu_rights_str_mv openAccess
rights_invalid_str_mv https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.format.none.fl_str_mv application/pdf
application/pdf
application/pdf
dc.publisher.none.fl_str_mv Chemical Industry Press
publisher.none.fl_str_mv Chemical Industry Press
dc.source.none.fl_str_mv reponame:CONICET Digital (CONICET)
instname:Consejo Nacional de Investigaciones Científicas y Técnicas
reponame_str CONICET Digital (CONICET)
collection CONICET Digital (CONICET)
instname_str Consejo Nacional de Investigaciones Científicas y Técnicas
repository.name.fl_str_mv CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicas
repository.mail.fl_str_mv dasensio@conicet.gov.ar; lcarlino@conicet.gov.ar
_version_ 1842269343919898624
score 13.13397

Publicaciones similares