Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. Applications

Autores
Cantero, Héctor; Baltanas, Miguel Angel; Grau, Ricardo José Antonio
Año de publicación
2000
Idioma
inglés
Tipo de recurso
artículo
Estado
versión publicada
Descripción
The behavior of an isothermal, vertical tube reactor in a dispersed bubble flow environment in either upflow, downflow or upflow-downflow configurations is examined, using the performance indicators defined in Part I. The hydrogenation of a coalescent organic system, like the one found in the mild hydrogenation process of soybean oil, is taken as a reference system. The likelihood of the axial changes of the local gas-slurry mass transfer efficiency and, then, of the controlling regimes of the process rate is discussed. Further effects of the configuration on the conversion of the liquid reactant, the unconverted mass of the gas phase, and the pressure drop are also analyzed.
Fil: Cantero, Héctor. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo Tecnológico para la Industria Química. Universidad Nacional del Litoral. Instituto de Desarrollo Tecnológico para la Industria Química; Argentina
Fil: Baltanas, Miguel Angel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo Tecnológico para la Industria Química. Universidad Nacional del Litoral. Instituto de Desarrollo Tecnológico para la Industria Química; Argentina
Fil: Grau, Ricardo José Antonio. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo Tecnológico para la Industria Química. Universidad Nacional del Litoral. Instituto de Desarrollo Tecnológico para la Industria Química; Argentina
Materia
Continuous Hydrogenation;
Performance Indicators;
Turbulent Tube Reactor;
Upflow-Downflow
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:11336/27702
Acceder
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oai_identifier_str oai:ri.conicet.gov.ar:11336/27702
network_acronym_str CONICETDig
repository_id_str 3498
network_name_str CONICET Digital (CONICET)
spelling Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. ApplicationsCantero, HéctorBaltanas, Miguel AngelGrau, Ricardo José AntonioContinuous Hydrogenation;Performance Indicators;Turbulent Tube Reactor;Upflow-Downflowhttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2The behavior of an isothermal, vertical tube reactor in a dispersed bubble flow environment in either upflow, downflow or upflow-downflow configurations is examined, using the performance indicators defined in Part I. The hydrogenation of a coalescent organic system, like the one found in the mild hydrogenation process of soybean oil, is taken as a reference system. The likelihood of the axial changes of the local gas-slurry mass transfer efficiency and, then, of the controlling regimes of the process rate is discussed. Further effects of the configuration on the conversion of the liquid reactant, the unconverted mass of the gas phase, and the pressure drop are also analyzed.Fil: Cantero, Héctor. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo Tecnológico para la Industria Química. Universidad Nacional del Litoral. Instituto de Desarrollo Tecnológico para la Industria Química; ArgentinaFil: Baltanas, Miguel Angel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo Tecnológico para la Industria Química. Universidad Nacional del Litoral. Instituto de Desarrollo Tecnológico para la Industria Química; ArgentinaFil: Grau, Ricardo José Antonio. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo Tecnológico para la Industria Química. Universidad Nacional del Litoral. Instituto de Desarrollo Tecnológico para la Industria Química; ArgentinaSoc Chemical Eng Japan2000-05info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/mswordapplication/pdfhttp://hdl.handle.net/11336/27702Cantero, Héctor; Baltanas, Miguel Angel; Grau, Ricardo José Antonio; Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. Applications; Soc Chemical Eng Japan; Journal Of Chemical Engineering Of Japan; 5-2000; 25-310021-9592CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/doi/10.1252/jcej.33.25info:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-10-22T11:23:56Zoai:ri.conicet.gov.ar:11336/27702instacron: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:34982025-10-22 11:23:56.755CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse
dc.title.none.fl_str_mv Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. Applications
title Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. Applications
spellingShingle Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. Applications
Cantero, Héctor
Continuous Hydrogenation;
Performance Indicators;
Turbulent Tube Reactor;
Upflow-Downflow
title_short Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. Applications
title_full Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. Applications
title_fullStr Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. Applications
title_full_unstemmed Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. Applications
title_sort Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. Applications
dc.creator.none.fl_str_mv Cantero, Héctor
Baltanas, Miguel Angel
Grau, Ricardo José Antonio
author Cantero, Héctor
author_facet Cantero, Héctor
Baltanas, Miguel Angel
Grau, Ricardo José Antonio
author_role author
author2 Baltanas, Miguel Angel
Grau, Ricardo José Antonio
author2_role author
author
dc.subject.none.fl_str_mv Continuous Hydrogenation;
Performance Indicators;
Turbulent Tube Reactor;
Upflow-Downflow
topic Continuous Hydrogenation;
Performance Indicators;
Turbulent Tube Reactor;
Upflow-Downflow
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 behavior of an isothermal, vertical tube reactor in a dispersed bubble flow environment in either upflow, downflow or upflow-downflow configurations is examined, using the performance indicators defined in Part I. The hydrogenation of a coalescent organic system, like the one found in the mild hydrogenation process of soybean oil, is taken as a reference system. The likelihood of the axial changes of the local gas-slurry mass transfer efficiency and, then, of the controlling regimes of the process rate is discussed. Further effects of the configuration on the conversion of the liquid reactant, the unconverted mass of the gas phase, and the pressure drop are also analyzed.
Fil: Cantero, Héctor. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo Tecnológico para la Industria Química. Universidad Nacional del Litoral. Instituto de Desarrollo Tecnológico para la Industria Química; Argentina
Fil: Baltanas, Miguel Angel. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo Tecnológico para la Industria Química. Universidad Nacional del Litoral. Instituto de Desarrollo Tecnológico para la Industria Química; Argentina
Fil: Grau, Ricardo José Antonio. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Desarrollo Tecnológico para la Industria Química. Universidad Nacional del Litoral. Instituto de Desarrollo Tecnológico para la Industria Química; Argentina
description The behavior of an isothermal, vertical tube reactor in a dispersed bubble flow environment in either upflow, downflow or upflow-downflow configurations is examined, using the performance indicators defined in Part I. The hydrogenation of a coalescent organic system, like the one found in the mild hydrogenation process of soybean oil, is taken as a reference system. The likelihood of the axial changes of the local gas-slurry mass transfer efficiency and, then, of the controlling regimes of the process rate is discussed. Further effects of the configuration on the conversion of the liquid reactant, the unconverted mass of the gas phase, and the pressure drop are also analyzed.
publishDate 2000
dc.date.none.fl_str_mv 2000-05
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/11336/27702
Cantero, Héctor; Baltanas, Miguel Angel; Grau, Ricardo José Antonio; Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. Applications; Soc Chemical Eng Japan; Journal Of Chemical Engineering Of Japan; 5-2000; 25-31
0021-9592
CONICET Digital
CONICET
url http://hdl.handle.net/11336/27702
identifier_str_mv Cantero, Héctor; Baltanas, Miguel Angel; Grau, Ricardo José Antonio; Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. II. Applications; Soc Chemical Eng Japan; Journal Of Chemical Engineering Of Japan; 5-2000; 25-31
0021-9592
CONICET Digital
CONICET
dc.language.none.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv info:eu-repo/semantics/altIdentifier/doi/10.1252/jcej.33.25
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/msword
application/pdf
dc.publisher.none.fl_str_mv Soc Chemical Eng Japan
publisher.none.fl_str_mv Soc Chemical Eng Japan
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_ 1846781772735447040
score 12.982451

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