Finding rigorous thermodynamic model parameters for the simulation of a reactive distillation column: case of ETBE production

Autores
Durruty, Gisela N.; Diaz, M. Soledad; Hoch, Patricia
Año de publicación
2014
Idioma
inglés
Tipo de recurso
documento de conferencia
Estado
versión publicada
Descripción
A model for a reactive distillation column for ETBE production was devel-oped using both a rigorous thermodynamic model (UNIFAC) and hydraulic constrains. The thermodynamic model included an activity coefficient approach for the liquid phase, UNIFAC, and ideal gas approximation for the vapor phase. The binary interaction parameters of UNIFAC were improved to better predict the equilibrium in the column. The binary interaction parameters were estimat-ed using experimental data taken from literature.
Sociedad Argentina de Informática e Investigación Operativa (SADIO)
Materia
Ciencias Informáticas
reactive distillation
ETBE
thermodynamics
Nivel de accesibilidad
acceso abierto
Condiciones de uso
http://creativecommons.org/licenses/by/3.0/
Repositorio
SEDICI (UNLP)
Institución
Universidad Nacional de La Plata
OAI Identificador
oai:sedici.unlp.edu.ar:10915/41998

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network_name_str SEDICI (UNLP)
spelling Finding rigorous thermodynamic model parameters for the simulation of a reactive distillation column: case of ETBE productionDurruty, Gisela N.Diaz, M. SoledadHoch, PatriciaCiencias Informáticasreactive distillationETBEthermodynamicsA model for a reactive distillation column for ETBE production was devel-oped using both a rigorous thermodynamic model (UNIFAC) and hydraulic constrains. The thermodynamic model included an activity coefficient approach for the liquid phase, UNIFAC, and ideal gas approximation for the vapor phase. The binary interaction parameters of UNIFAC were improved to better predict the equilibrium in the column. The binary interaction parameters were estimat-ed using experimental data taken from literature.Sociedad Argentina de Informática e Investigación Operativa (SADIO)2014-09info:eu-repo/semantics/conferenceObjectinfo:eu-repo/semantics/publishedVersionObjeto de conferenciahttp://purl.org/coar/resource_type/c_5794info:ar-repo/semantics/documentoDeConferenciaapplication/pdf185-195http://sedici.unlp.edu.ar/handle/10915/41998enginfo:eu-repo/semantics/altIdentifier/url/http://43jaiio.sadio.org.ar/proceedings/SII/16_Durruty%20et%20al..pdfinfo:eu-repo/semantics/altIdentifier/issn/2313-9102info:eu-repo/semantics/openAccesshttp://creativecommons.org/licenses/by/3.0/Creative Commons Attribution 3.0 Unported (CC BY 3.0)reponame:SEDICI (UNLP)instname:Universidad Nacional de La Platainstacron:UNLP2025-10-15T10:53:46Zoai:sedici.unlp.edu.ar:10915/41998Institucionalhttp://sedici.unlp.edu.ar/Universidad públicaNo correspondehttp://sedici.unlp.edu.ar/oai/snrdalira@sedici.unlp.edu.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:13292025-10-15 10:53:47.001SEDICI (UNLP) - Universidad Nacional de La Platafalse
dc.title.none.fl_str_mv Finding rigorous thermodynamic model parameters for the simulation of a reactive distillation column: case of ETBE production
title Finding rigorous thermodynamic model parameters for the simulation of a reactive distillation column: case of ETBE production
spellingShingle Finding rigorous thermodynamic model parameters for the simulation of a reactive distillation column: case of ETBE production
Durruty, Gisela N.
Ciencias Informáticas
reactive distillation
ETBE
thermodynamics
title_short Finding rigorous thermodynamic model parameters for the simulation of a reactive distillation column: case of ETBE production
title_full Finding rigorous thermodynamic model parameters for the simulation of a reactive distillation column: case of ETBE production
title_fullStr Finding rigorous thermodynamic model parameters for the simulation of a reactive distillation column: case of ETBE production
title_full_unstemmed Finding rigorous thermodynamic model parameters for the simulation of a reactive distillation column: case of ETBE production
title_sort Finding rigorous thermodynamic model parameters for the simulation of a reactive distillation column: case of ETBE production
dc.creator.none.fl_str_mv Durruty, Gisela N.
Diaz, M. Soledad
Hoch, Patricia
author Durruty, Gisela N.
author_facet Durruty, Gisela N.
Diaz, M. Soledad
Hoch, Patricia
author_role author
author2 Diaz, M. Soledad
Hoch, Patricia
author2_role author
author
dc.subject.none.fl_str_mv Ciencias Informáticas
reactive distillation
ETBE
thermodynamics
topic Ciencias Informáticas
reactive distillation
ETBE
thermodynamics
dc.description.none.fl_txt_mv A model for a reactive distillation column for ETBE production was devel-oped using both a rigorous thermodynamic model (UNIFAC) and hydraulic constrains. The thermodynamic model included an activity coefficient approach for the liquid phase, UNIFAC, and ideal gas approximation for the vapor phase. The binary interaction parameters of UNIFAC were improved to better predict the equilibrium in the column. The binary interaction parameters were estimat-ed using experimental data taken from literature.
Sociedad Argentina de Informática e Investigación Operativa (SADIO)
description A model for a reactive distillation column for ETBE production was devel-oped using both a rigorous thermodynamic model (UNIFAC) and hydraulic constrains. The thermodynamic model included an activity coefficient approach for the liquid phase, UNIFAC, and ideal gas approximation for the vapor phase. The binary interaction parameters of UNIFAC were improved to better predict the equilibrium in the column. The binary interaction parameters were estimat-ed using experimental data taken from literature.
publishDate 2014
dc.date.none.fl_str_mv 2014-09
dc.type.none.fl_str_mv info:eu-repo/semantics/conferenceObject
info:eu-repo/semantics/publishedVersion
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info:ar-repo/semantics/documentoDeConferencia
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status_str publishedVersion
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dc.language.none.fl_str_mv eng
language eng
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dc.rights.none.fl_str_mv info:eu-repo/semantics/openAccess
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eu_rights_str_mv openAccess
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