Trickle-Bed Laboratory Reactors for Kinetic studies

Trickle-Bed Laboratory Reactors for Kinetic studies

ID:40111092

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頁(yè)數(shù):70頁(yè)

時(shí)間:2019-07-21

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1、INTERNATIONALJOURNALOFCHEMICALREACTORENGINEERINGVolume72009ReviewR2Trickle-BedLaboratoryReactorsforKineticStudiesGaetanMaryJamalChaoukiyFrancisLuckzEcolePolytechniquedeMontreal,gaetan.mary@polymtl.cayEcolePolytechniquedeMontreal,jamal.chaouki@polymtl.ca

2、zTotalS.A.,francis.luck@total.comISSN1542-6580Broughttoyouby

3、WenzhouUniversityAuthenticated

4、218.75.16.101DownloadDate

5、9/22/123:01PMTrickle-BedLaboratoryReactorsforKineticStudiesGaetanMary,JamalChaouki,andFrancisLuckAbstractInthispaper,differentphenomenaaf

6、fectinglaboratorytrickle-bedreactorsarecarefullyreviewed.Beforefocusingonlaboratoryscale,somegeneralconsider-ationsabouttrickle-bedreactorsarediscussed:regimes,industrialuses,etc.Themainfactorsalaboratorytricklebedreactorsarepresentedanddetailed.Thegreate

7、stsixfactorsinclude:homogeneityofthecatalystbed,catalystwetting,axialdispersion,channeling,isothermicityandmasstransfer.Thesefactorsarereviewedanddifferentcriteria,suggestedintheliterature,aregiveninordertominimizethein?uenceofthesesixfactors;foreachcrite

8、rion,asimpleapplica-tionispresented.Finally,theapplicationofallthecriteriagiveninthepaperisbasedonahypotheticalexample(hydrodesulfurization).KEYWORDS:trickle-bedreactors,laboratoryscale,plug?owreactors,catalystwetting,axialdispersion,masstransfer,isotherm

9、icity,channeling,homogeneity,bedofcatalystBroughttoyouby

10、WenzhouUniversityAuthenticated

11、218.75.16.101DownloadDate

12、9/22/123:01PMMaryetal.:Trickle-BedLaboratoryReactorsforKineticStudies11.IntroductionSlurryandtrickle-bedreactorsarethetwomaintypesofthree-pha

13、sereactors.Theyareusedinindustrialunitsforconductingsolid-catalyzedreactions.Inslurryreactors,thecatalystissuspendedinafluid.Itsvolumerepresentingabout1to20%ofthetotalvolumeofthereactoranditsdiameterisaround0.1millimeters.Trickle-bedreactorsarepackedbedre

14、actors.Wherethecatalystoccupiesabout50%ofthetotalvolume,theparticlediameterisaround1centimeterindiameterandthetwofluids(gasandliquid)areflowinginsideandwettingthebed(TrambouzeandEuzen,2002;Harriot,2003).Commonflowco

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