dc.contributorUniversidade Estadual Paulista (Unesp)
dc.contributorUniversity of British Columbia Department of Chemical and Biological Engineering
dc.date.accessioned2014-05-20T15:16:09Z
dc.date.available2014-05-20T15:16:09Z
dc.date.created2014-05-20T15:16:09Z
dc.date.issued2004-01-01
dc.identifierBrazilian Journal of Chemical Engineering. Brazilian Society of Chemical Engineering, v. 21, n. 1, p. 13-22, 2004.
dc.identifier0104-6632
dc.identifierhttp://hdl.handle.net/11449/29926
dc.identifier10.1590/S0104-66322004000100003
dc.identifierS0104-66322004000100003
dc.identifierS0104-66322004000100003.pdf
dc.description.abstractExperimental heat transfer studies were carried out in 50.8 mm diameter packed beds of glass beads percolated by water and heated from the wall. The tube-to-particle diameter ratio (D/d p) ranged from 1.72 to 13.7 and the water flow rate from 1.1 to 9.9 l/min. Bed heights ranged from 100 mm to 700 mm. The radial temperature was measured above the bed surface by five aligned sheathed thermocouples. Variations in angular temperature were observed, independent of both radial position and particle diameter. Results of repeated tests with the same packing and with repacking did not differ statistically. The radial temperature profile at the bed entrance, measured by a ring-shaped sensor, was uniform except very close to the tube wall.
dc.languageeng
dc.publisherBrazilian Society of Chemical Engineering
dc.relationBrazilian Journal of Chemical Engineering
dc.relation0.925
dc.relation0,395
dc.rightsAcesso aberto
dc.sourceSciELO
dc.subjectheat transfer
dc.subjectone-phase water flow
dc.subjectradial temperature profile
dc.titleHeat transfer in packed beds: experimental evaluation of one-phase water flow
dc.typeArtículos de revistas


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