You are in the accessibility menu

Please use this identifier to cite or link to this item: http://acervodigital.unesp.br/handle/11449/34644
Full metadata record
DC FieldValueLanguage
dc.contributor.authorThomeo, J. C.-
dc.contributor.authorFreire, J. T.-
dc.date.accessioned2014-05-20T15:23:59Z-
dc.date.accessioned2016-10-25T17:58:01Z-
dc.date.available2014-05-20T15:23:59Z-
dc.date.available2016-10-25T17:58:01Z-
dc.date.issued2000-06-01-
dc.identifierhttp://dx.doi.org/10.1016/S0009-2509(99)00465-0-
dc.identifier.citationChemical Engineering Science. Oxford: Pergamon-Elsevier B.V., v. 55, n. 12, p. 2329-2338, 2000.-
dc.identifier.issn0009-2509-
dc.identifier.urihttp://hdl.handle.net/11449/34644-
dc.identifier.urihttp://acervodigital.unesp.br/handle/11449/34644-
dc.description.abstractStudies have been carried out on the heat transfer in a packed bed of glass beads percolated by air at moderate flow rates. Rigorous statistic analysis of the experimental data was carried out and the traditional two parameter model was used to represent them. The parameters estimated were the effective radial thermal conductivity, k, and the wall coefficient, h, through the least squares method. The results were evaluated as to the boundary bed inlet temperature, T-o, number of terms of the solution series and number of experimental points used in the estimate. Results indicated that a small difference in T-o was sufficient to promote great modifications in the estimated parameters and in the statistical properties of the model. The use of replicas at points of high parametric information of the model improved the results, although analysis of the residuals has resulted in the rejection of this alternative. In order to evaluate cion-linearity of the model, Bates and Watts (1988) curvature measurements and the Box (1971) biases of the coefficients were calculated. The intrinsic curvatures of the model (IN) tend to be concentrated at low bed heights and those due to parameter effects (PE) are spread all over the bed. The Box biases indicated both parameters as responsible for the curvatures PE, h being somewhat more problematic. (C) 2000 Elsevier B.V. Ltd. All rights reserved.en
dc.format.extent2329-2338-
dc.language.isoeng-
dc.publisherElsevier B.V.-
dc.sourceWeb of Science-
dc.subjectheat transferpt
dc.subjectporous mediapt
dc.subjectpacked bedspt
dc.subjectpseudo-homogeneous modelpt
dc.subjectparameter estimationpt
dc.subjectmodel non-linearitypt
dc.titleHeat transfer in fixed bed: a model non-linearity approachen
dc.typeoutro-
dc.contributor.institutionUniversidade Estadual Paulista (UNESP)-
dc.contributor.institutionUniversidade Federal de São Carlos (UFSCar)-
dc.description.affiliationUniv Estadual Paulista, Dept Engn & Tecnol Alimentos, BR-15054000 SJ do Rio Preto, SP, Brazil-
dc.description.affiliationUniv Fed Sao Carlos, Dept Engn Quim, BR-13565905 Sao Carlos, SP, Brazil-
dc.description.affiliationUnespUniv Estadual Paulista, Dept Engn & Tecnol Alimentos, BR-15054000 SJ do Rio Preto, SP, Brazil-
dc.identifier.doi10.1016/S0009-2509(99)00465-0-
dc.identifier.wosWOS:000086159600019-
dc.rights.accessRightsAcesso restrito-
dc.relation.ispartofChemical Engineering Science-
Appears in Collections:Artigos, TCCs, Teses e Dissertações da Unesp

There are no files associated with this item.
 

Items in DSpace are protected by copyright, with all rights reserved, unless otherwise indicated.