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Particle-fluid mass transfer in multiparticle systems at low Reynolds numbers

Academic Article
Publication Date:
2013
abstract:
The problemofmasstransferbetweenactivesolidparticlesandafluidinmultiparticlesystemsis examinedwithafocusonthestagnantandthelowReynoldsnumbercases.Thisproblemhasattracted significantattentionwithregardtooperationoffixedandfluidizedbeds.Itisrecognizedthatdifferent Sherwoodnumberscanbedefineddependingonthechoiceofthereferenceconcentrationdifference (drivingforce).Aneffective Sh has oftenbeenusedtoanalyzeexperimentaldatabasedonanoverall concentrationdifferenceacrossthebed.Alocal Sh can alsobeintroducedbasedonaconcentration differenceclosetotheactiveparticle.However,theuseofthesetwodifferentSherwoodnumbers impliesadifferentimplementationofthemassbalanceequations. The massbalanceequationsarehereanalyticallysolvedbothunderstagnantandnon-stagnant conditionsinamultiparticlesystemundersuitablesimplifyingassumptions.Equationsfortheeffective and localSherwoodnumbersarederivedforthegeneralcaseandfortheasymptoticlimits.Allowance is givenforthevariationofbedvoidageandvolumefractionofactiveparticlesinthebed.Itisshown that thelocal Sh only dependsongeometricalandfluid-dynamicsconsiderationsandaccordinglyhasa generalvalidity.Onthecontrary,theeffective Sh also dependsontheassumptionsmadeinderivingthe mass balanceequationsacrossthebed(e.g.,fluidplugflow).Theuseofthelocal Sh is therefore suggested. Resultsshowthatfor Re-0 thelimitingvalueofthelocal Sh is alwaysafinitenumber,whilethe effective Sh tendstozerolinearlywith Re. Itisshownthatthisresultissimplyaconsequenceofthe plug flowassumptionmadeinthebedmassbalance.Thegeneralexpressionsderivedherecompare very welltoexperimentaltrendsforthecasesoflargeReynoldsnumbersandoffewisolatedactive spheres immersedinabedofinertparticles,wheremostofthereportedexperimentaldatagather. Unfortunately,forthemostcontroversialcaseofverylow Re in bedsmadeentirelyofactiveparticlesno reliabledataappearstobeavailabletochecktheaccuracyoftheexpressions.
Iris type:
01.01 Articolo in rivista
Keywords:
Mass transfer; Sherwood number; Multiphase flow; Diffusion; Packed bed
List of contributors:
Scala, Fabrizio
Handle:
https://iris.cnr.it/handle/20.500.14243/124282
Published in:
CHEMICAL ENGINEERING SCIENCE
Journal
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