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dc.creatorStakić, M.
dc.creatorBanjac, M.
dc.creatorUrošević, Tijana
dc.date.accessioned2020-12-17T20:08:26Z
dc.date.available2020-12-17T20:08:26Z
dc.date.issued2011
dc.identifier.issn0104-6632
dc.identifier.urihttp://aspace.agrif.bg.ac.rs/handle/123456789/2607
dc.description.abstractThe paper addresses numerical simulation for the case of convective drying of hygroscopic material in a packed bed, analyzing agreement between the simulated and the corresponding experimental results. In the simulation model of unsteady simultaneous one-dimensional heat and mass transfer between gas phase and dried material, it is assumed that the gas-solid interface is at thermodynamic equilibrium, while the drying rate of the specific product is calculated by applying the concept of a "drying coefficient". Model validation was clone on the basis of the experimental data obtained with potato cubes. The obtained drying kinetics, both experimental and numerical, show that higher gas (drying agent) velocities (flow-rates), as well as lower equivalent grain diameters, induce faster drying. This effect is more pronounced for deeper beds, because of the larger amount of wet material to be dried using the same drying agent capacity.en
dc.publisherBrazilian Soc Chemical Eng, Sao Paulo
dc.rightsopenAccess
dc.rights.urihttps://creativecommons.org/licenses/by/4.0/
dc.sourceBrazilian Journal of Chemical Engineering
dc.subjectHeat and mass transferen
dc.subjectMathematical modelen
dc.subjectSimulationen
dc.titleNumerical study on hygroscopic material drying in packed beden
dc.typearticle
dc.rights.licenseBY
dc.citation.epage284
dc.citation.issue2
dc.citation.other28(2): 273-284
dc.citation.rankM23
dc.citation.spage273
dc.citation.volume28
dc.identifier.doi10.1590/S0104-66322011000200012
dc.identifier.fulltexthttp://aspace.agrif.bg.ac.rs/bitstream/id/1366/2604.pdf
dc.identifier.scopus2-s2.0-79960497606
dc.identifier.wos000291123900012
dc.type.versionpublishedVersion


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Приказ основних података о документу