dc.contributorUniversidade Estadual Paulista (Unesp)
dc.contributorCOSAN SA Ind & Comercio
dc.contributorUniversidade Federal de Viçosa (UFV)
dc.date.accessioned2014-05-20T14:02:07Z
dc.date.accessioned2022-10-05T14:49:42Z
dc.date.available2014-05-20T14:02:07Z
dc.date.available2022-10-05T14:49:42Z
dc.date.created2014-05-20T14:02:07Z
dc.date.issued2012-01-15
dc.identifierBiochemical Engineering Journal. Lausanne: Elsevier B.V. Sa, v. 60, p. 111-118, 2012.
dc.identifier1369-703X
dc.identifierhttp://hdl.handle.net/11449/21903
dc.identifier10.1016/j.bej.2011.10.011
dc.identifierWOS:000300205700018
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/3895610
dc.description.abstractSugarcane (Saccharum sp.) is a relatively low-cost agricultural resource, produced mainly in tropical and subtropical regions of the planet. One of the most important applications of sugarcane juice is in the production of ethanol biofuel. A correct design of unit operations during the sugarcane juice processing requires an accurate characterization of the flow properties (friction factors, rheological behaviour, thermophysical properties and heat transfer coefficients) of this raw material. In this work, friction factors (f) and Nusselt number (Nu) were determined for sugarcane juice in different steps of its processing (untreated sugarcane juice, clarified sugarcane juice and mixed sugarcane juice). For both laminar and turbulent flows, the empirical models for f fitted well (r(2) >= 0.9) with the experimental values obtained by pressure drop measurements. Also. Nu values calculated by applying the empirical correlation of Hausen (for laminar flow) and that of Sieder-Tate (for turbulent flow) presented good adjustment (r(2) >= 0.9) to the experimentally determined values. Thus, the f and Nu values obtained for turbulent flow were taken to verify the Colburn analogy, which furnished results with small deviations (<= 8.9%) from the expected ideal value. This finding indicates the suitability of such analogy in this case, allowing good estimations of heat transfer coefficients from frictions factors, or vice versa, for sugarcane juices in turbulent flow conditions. (C) 2011 Elsevier B.V. All rights reserved.
dc.languageeng
dc.publisherElsevier B.V. Sa
dc.relationBiochemical Engineering Journal
dc.relation3.226
dc.rightsAcesso restrito
dc.sourceWeb of Science
dc.subjectBiofuel
dc.subjectColburn analogy
dc.subjectEthanol
dc.subjectFriction factor
dc.subjectHeat transfer
dc.subjectSugarcane
dc.titleFriction factors, convective heat transfer coefficients and the Colburn analogy for industrial sugarcane juices
dc.typeArtigo


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