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dc.creatorCantero, Héctor-
dc.creatorGrau, Ricardo José Antonio-
dc.creatorBaltanas, Miguel Angel-
dc.date2017-11-07T11:52:28Z-
dc.date2017-11-07T11:52:28Z-
dc.date2000-05-
dc.date2017-11-03T20:26:31Z-
dc.date.accessioned2019-04-29T15:40:35Z-
dc.date.available2019-04-29T15:40:35Z-
dc.date.issued2017-11-07T11:52:28Z-
dc.date.issued2017-11-07T11:52:28Z-
dc.date.issued2000-05-
dc.date.issued2017-11-03T20:26:31Z-
dc.identifierCantero, Héctor; Grau, Ricardo José Antonio; Baltanas, Miguel Angel; Interaction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. I. Performance Indicators; Soc Chemical Eng Japan; Journal Of Chemical Engineering Of Japan; 33; 1; 5-2000; 19-24-
dc.identifier0021-9592-
dc.identifierhttp://hdl.handle.net/11336/27701-
dc.identifierCONICET Digital-
dc.identifierCONICET-
dc.identifier.urihttp://rodna.bn.gov.ar:8080/jspui/handle/bnmm/299231-
dc.descriptionTo analyze the performance of a vertical tube reactor involving a gas-slurry reacting system in dispersed bubble flow and upflow, downflow, and upflow-downflow (alternating) configurations, several performance indicators are defined and expressed in terms of integral equations. A local effectiveness factor associated with the efficiency for gas-slurry mass transfer, conversion of the liquid reactant, the local unconverted mass fraction of the gas phase, and the pressure drop are taken as performance indicators. Bounding criteria for diffusion-controlled and chemical reaction-controlled regimes are established, and their transitions along the reactor are also discussed. A generic heterogeneous catalytic hydrogenation, exemplified by the single reaction A(l) + H2(g) -> B(l), is taken as a suitable reference system.-
dc.descriptionFil: 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-
dc.descriptionFil: 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-
dc.descriptionFil: 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-
dc.formatapplication/pdf-
dc.formatapplication/msword-
dc.formatapplication/pdf-
dc.languageeng-
dc.publisherSoc Chemical Eng Japan-
dc.relationinfo:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1252/jcej.33.19-
dc.rightsinfo:eu-repo/semantics/restrictedAccess-
dc.rightshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/-
dc.sourcereponame:CONICET Digital (CONICET)-
dc.sourceinstname:Consejo Nacional de Investigaciones Científicas y Técnicas-
dc.sourceinstacron:CONICET-
dc.subjectControlling regimes;-
dc.subjectPerformance indicators;-
dc.subjectTurbulent tube reactor;-
dc.subjectUpflow-downflow-
dc.subjectOtras Ingeniería Química-
dc.subjectIngeniería Química-
dc.subjectINGENIERÍAS Y TECNOLOGÍAS-
dc.titleInteraction Between Hydrodynamics and Chemical Reaction Rate in a Vertical Gas-Slurry Cocurrent Turbulent Tube Reactor. I. Performance Indicators-
dc.typeinfo:eu-repo/semantics/article-
dc.typeinfo:eu-repo/semantics/publishedVersion-
dc.typeinfo:ar-repo/semantics/articulo-
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