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Please use this identifier to cite or link to this item: http://acervodigital.unesp.br/handle/11449/67801
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dc.contributor.authorThoméo, João C.-
dc.contributor.authorRouiller, Cláudia O.-
dc.contributor.authorFreire, José T.-
dc.date.accessioned2014-05-27T11:21:07Z-
dc.date.accessioned2016-10-25T18:19:44Z-
dc.date.available2014-05-27T11:21:07Z-
dc.date.available2016-10-25T18:19:44Z-
dc.date.issued2004-07-21-
dc.identifierhttp://dx.doi.org/10.1021/ie030759u-
dc.identifier.citationIndustrial and Engineering Chemistry Research, v. 43, n. 15, p. 4140-4148, 2004.-
dc.identifier.issn0888-5885-
dc.identifier.urihttp://hdl.handle.net/11449/67801-
dc.identifier.urihttp://acervodigital.unesp.br/handle/11449/67801-
dc.description.abstractHeat-transfer studies were carried out in a packed bed of glass beads, cooled by the wall, through which air percolated. Tube-to-particle diameter ratios (D/dp) ranged from 1.8 to 55, while the air mass flux ranged from 0.204 to 2.422 kg/m2·s. The outlet bed temperature (TL) was measured by a brass ring-shaped sensor and by aligned thermocouples. The resulting radial temperature profiles differed statistically. Angular temperature fluctuations were observed through measurements made at 72 angular positions. These fluctuations do not follow a normal distribution around the mean for low ratios D/dp. The presence of a restraining screen, as well as the increasing distance between the temperature measuring device and the bed surface, distorts TL. The radial temperature profile at the bed entrance (T0) was measured by a ring-shaped sensor, and T 0 showed to be a function of the radial position, the particle diameter, and the fluid flow rate.en
dc.format.extent4140-4148-
dc.language.isoeng-
dc.sourceScopus-
dc.subjectCooling-
dc.subjectFlow of fluids-
dc.subjectGlass-
dc.subjectHeat transfer-
dc.subjectThermocouples-
dc.subjectAir flow-
dc.subjectTemperature profiles-
dc.subjectPacked beds-
dc.subjectglass-
dc.subjectmicrosphere-
dc.subjectair-
dc.subjectairflow-
dc.subjectheat transfer-
dc.subjectmathematical analysis-
dc.subjectmodel-
dc.subjectpacked bed-
dc.subjectair mass flux-
dc.subjectanalysis-
dc.subjectexperiment-
dc.subjectflow rate-
dc.subjectmass-
dc.subjectmeasurement-
dc.subjectpacked bed reactor-
dc.subjectparticle size-
dc.subjectradial temperature-
dc.subjectsensor-
dc.subjecttemperature-
dc.subjecttube-
dc.subjecttube to particle diameter ratio-
dc.titleExperimental analysis of heat transfer in packed beds with air flowen
dc.typeoutro-
dc.contributor.institutionUniversidade Estadual Paulista (UNESP)-
dc.contributor.institutionUniversidade Federal de São Carlos (UFSCar)-
dc.description.affiliationDepto. Engenharia/Tecn. Alimentos Universidade Estadual Paulista, Rua Cristovao Colombo 2265, Sao Jose do Rio Preto SP, 15054-000-
dc.description.affiliationDepartamento de Engenharia Quimica Universidade Federal de Sao Carlos, Rod Washington Luiz km 235, Sao Carlos SP, 13565-905-
dc.description.affiliationUnespDepto. Engenharia/Tecn. Alimentos Universidade Estadual Paulista, Rua Cristovao Colombo 2265, Sao Jose do Rio Preto SP, 15054-000-
dc.identifier.doi10.1021/ie030759u-
dc.identifier.wosWOS:000222738000018-
dc.rights.accessRightsAcesso restrito-
dc.relation.ispartofIndustrial and Engineering Chemistry Research-
dc.identifier.scopus2-s2.0-3242686914-
Appears in Collections:Artigos, TCCs, Teses e Dissertações da Unesp

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