Thermodynamic Properties for the Simulation of Crude Oil Primary Refining

Autores
Gutierrez, Juan Pablo; Benitez, Leonel Alberto; Martínez, Julieta; Ale Ruiz, Liliana; Erdmann, Eleonora
Año de publicación
2014
Idioma
inglés
Tipo de recurso
artículo
Estado
versión publicada
Descripción
Commonly, the use of simulators in the industry is performed without having a proper theoretical support. Sometimes this situation is a consequence of both, lack of time and the dairy dynamism required in the refinery industries. Particularly, the application of thermodynamic models is often not properly considered for the specific process under analysis. An undesirable fact can appear, for example, when a wrong properties package is chosen or even more when this selection step is completely ignored. The aim of this article is to prove that the habitual selection of the thermodynamic models is appropriate or not for the primary refining process. For the purpose, two available simulation softwares and thermodynamic models have been analyzed. The research paper focuses on establishing a guide for plant operators with information that has been previously proven, with theoretical support. In particular, for the oil crude atmospheric distillation (Topping), engineers use almost by default the Peng– Robinson thermodynamic package in Aspen Hysys simulator and Chao–Seader in Aspen Plus. Although the use of the thermodynamic property packages involves a whole theoretical support, this is not considered at the time of their election.
Fil: Gutierrez, Juan Pablo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Salta. Instituto de Investigación para la Industria Química (i); Argentina
Fil: Benitez, Leonel Alberto. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Salta. Instituto de Investigación Para la Industria Química (i); Argentina
Fil: Martínez, Julieta. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Salta. Instituto de Investigación para la Industria Química (i); Argentina
Fil: Ale Ruiz, Liliana. Universidad Nacional de Salta. Facultad de Ingenieria; Argentina
Fil: Erdmann, Eleonora. Instituto Tecnologico de Buenos Aires; Argentina
Materia
Crude oil
Distillation
Simulation
Thermodynamic Properties
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:11336/7756
Acceder
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spelling Thermodynamic Properties for the Simulation of Crude Oil Primary RefiningGutierrez, Juan PabloBenitez, Leonel AlbertoMartínez, JulietaAle Ruiz, LilianaErdmann, EleonoraCrude oilDistillationSimulationThermodynamic Propertieshttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2Commonly, the use of simulators in the industry is performed without having a proper theoretical support. Sometimes this situation is a consequence of both, lack of time and the dairy dynamism required in the refinery industries. Particularly, the application of thermodynamic models is often not properly considered for the specific process under analysis. An undesirable fact can appear, for example, when a wrong properties package is chosen or even more when this selection step is completely ignored. The aim of this article is to prove that the habitual selection of the thermodynamic models is appropriate or not for the primary refining process. For the purpose, two available simulation softwares and thermodynamic models have been analyzed. The research paper focuses on establishing a guide for plant operators with information that has been previously proven, with theoretical support. In particular, for the oil crude atmospheric distillation (Topping), engineers use almost by default the Peng– Robinson thermodynamic package in Aspen Hysys simulator and Chao–Seader in Aspen Plus. Although the use of the thermodynamic property packages involves a whole theoretical support, this is not considered at the time of their election.Fil: Gutierrez, Juan Pablo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Salta. Instituto de Investigación para la Industria Química (i); ArgentinaFil: Benitez, Leonel Alberto. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Salta. Instituto de Investigación Para la Industria Química (i); ArgentinaFil: Martínez, Julieta. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Salta. Instituto de Investigación para la Industria Química (i); ArgentinaFil: Ale Ruiz, Liliana. Universidad Nacional de Salta. Facultad de Ingenieria; ArgentinaFil: Erdmann, Eleonora. Instituto Tecnologico de Buenos Aires; ArgentinaIJERA2014-04info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/7756Gutierrez, Juan Pablo; Benitez, Leonel Alberto; Martínez, Julieta; Ale Ruiz, Liliana; Erdmann, Eleonora; Thermodynamic Properties for the Simulation of Crude Oil Primary Refining; IJERA; International Journal of Engineering Research and Applications; 4; 4; 4-2014; 190-1942248-9622enginfo:eu-repo/semantics/altIdentifier/url/http://www.ijera.com/papers/Vol4_issue4/Version%201/AA044190194.pdfinfo:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-09-03T09:46:18Zoai:ri.conicet.gov.ar:11336/7756instacron: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 09:46:18.407CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse
dc.title.none.fl_str_mv Thermodynamic Properties for the Simulation of Crude Oil Primary Refining
title Thermodynamic Properties for the Simulation of Crude Oil Primary Refining
spellingShingle Thermodynamic Properties for the Simulation of Crude Oil Primary Refining
Gutierrez, Juan Pablo
Crude oil
Distillation
Simulation
Thermodynamic Properties
title_short Thermodynamic Properties for the Simulation of Crude Oil Primary Refining
title_full Thermodynamic Properties for the Simulation of Crude Oil Primary Refining
title_fullStr Thermodynamic Properties for the Simulation of Crude Oil Primary Refining
title_full_unstemmed Thermodynamic Properties for the Simulation of Crude Oil Primary Refining
title_sort Thermodynamic Properties for the Simulation of Crude Oil Primary Refining
dc.creator.none.fl_str_mv Gutierrez, Juan Pablo
Benitez, Leonel Alberto
Martínez, Julieta
Ale Ruiz, Liliana
Erdmann, Eleonora
author Gutierrez, Juan Pablo
author_facet Gutierrez, Juan Pablo
Benitez, Leonel Alberto
Martínez, Julieta
Ale Ruiz, Liliana
Erdmann, Eleonora
author_role author
author2 Benitez, Leonel Alberto
Martínez, Julieta
Ale Ruiz, Liliana
Erdmann, Eleonora
author2_role author
author
author
author
dc.subject.none.fl_str_mv Crude oil
Distillation
Simulation
Thermodynamic Properties
topic Crude oil
Distillation
Simulation
Thermodynamic Properties
purl_subject.fl_str_mv https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
dc.description.none.fl_txt_mv Commonly, the use of simulators in the industry is performed without having a proper theoretical support. Sometimes this situation is a consequence of both, lack of time and the dairy dynamism required in the refinery industries. Particularly, the application of thermodynamic models is often not properly considered for the specific process under analysis. An undesirable fact can appear, for example, when a wrong properties package is chosen or even more when this selection step is completely ignored. The aim of this article is to prove that the habitual selection of the thermodynamic models is appropriate or not for the primary refining process. For the purpose, two available simulation softwares and thermodynamic models have been analyzed. The research paper focuses on establishing a guide for plant operators with information that has been previously proven, with theoretical support. In particular, for the oil crude atmospheric distillation (Topping), engineers use almost by default the Peng– Robinson thermodynamic package in Aspen Hysys simulator and Chao–Seader in Aspen Plus. Although the use of the thermodynamic property packages involves a whole theoretical support, this is not considered at the time of their election.
Fil: Gutierrez, Juan Pablo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Salta. Instituto de Investigación para la Industria Química (i); Argentina
Fil: Benitez, Leonel Alberto. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Salta. Instituto de Investigación Para la Industria Química (i); Argentina
Fil: Martínez, Julieta. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Salta. Instituto de Investigación para la Industria Química (i); Argentina
Fil: Ale Ruiz, Liliana. Universidad Nacional de Salta. Facultad de Ingenieria; Argentina
Fil: Erdmann, Eleonora. Instituto Tecnologico de Buenos Aires; Argentina
description Commonly, the use of simulators in the industry is performed without having a proper theoretical support. Sometimes this situation is a consequence of both, lack of time and the dairy dynamism required in the refinery industries. Particularly, the application of thermodynamic models is often not properly considered for the specific process under analysis. An undesirable fact can appear, for example, when a wrong properties package is chosen or even more when this selection step is completely ignored. The aim of this article is to prove that the habitual selection of the thermodynamic models is appropriate or not for the primary refining process. For the purpose, two available simulation softwares and thermodynamic models have been analyzed. The research paper focuses on establishing a guide for plant operators with information that has been previously proven, with theoretical support. In particular, for the oil crude atmospheric distillation (Topping), engineers use almost by default the Peng– Robinson thermodynamic package in Aspen Hysys simulator and Chao–Seader in Aspen Plus. Although the use of the thermodynamic property packages involves a whole theoretical support, this is not considered at the time of their election.
publishDate 2014
dc.date.none.fl_str_mv 2014-04
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/11336/7756
Gutierrez, Juan Pablo; Benitez, Leonel Alberto; Martínez, Julieta; Ale Ruiz, Liliana; Erdmann, Eleonora; Thermodynamic Properties for the Simulation of Crude Oil Primary Refining; IJERA; International Journal of Engineering Research and Applications; 4; 4; 4-2014; 190-194
2248-9622
url http://hdl.handle.net/11336/7756
identifier_str_mv Gutierrez, Juan Pablo; Benitez, Leonel Alberto; Martínez, Julieta; Ale Ruiz, Liliana; Erdmann, Eleonora; Thermodynamic Properties for the Simulation of Crude Oil Primary Refining; IJERA; International Journal of Engineering Research and Applications; 4; 4; 4-2014; 190-194
2248-9622
dc.language.none.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv info:eu-repo/semantics/altIdentifier/url/http://www.ijera.com/papers/Vol4_issue4/Version%201/AA044190194.pdf
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
application/pdf
dc.publisher.none.fl_str_mv IJERA
publisher.none.fl_str_mv IJERA
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
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score 13.13397

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