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Title Effect of particle density on the fluidity of a fluidized catalyst bed and evaluation of fluidity
Creator/Author Yusui, T. ; Miyauchi, T. ; Tsutusi, T.
Publication Date1985 Jul 01
OSTI IdentifierOSTI ID: 5074302
Other Number(s)CODEN: INCEA
Resource TypeJournal Article
Resource RelationInt. Chem. Eng. ; Vol/Issue: 25:3
Research OrgDepartment of Chemical Engineering, Faculty of Engineering, University of Tokyo, Tokyo
Subject420400 -- Engineering-- Heat Transfer & Fluid Flow; CATALYSTS-- PARTICLE SIZE;FLUIDIZED BEDS-- CATALYSTS;FLUIDIZED BEDS-- HYDRAULIC CONDUCTIVITY;FLUIDIZED BEDS-- HYDRAULICS; DENSITY;FLOW RATE;GAS FLOW;WEIGHT
Related SubjectFLUID FLOW;FLUID MECHANICS;MECHANICS;PHYSICAL PROPERTIES;SIZE
Description/Abstract The states of fluidization of FCC particles and two other types of particles with almost the same mean particle size, size distribution, and weight fraction of <44-..mu..m fines, but of higher density, were studied in beds 5.2-50 cm in internal diameter at superficial gas velocities up to about 60 cm/s.^The FCC particles fluidized smoothly, but the denser particles resulted in severe channeling in deep beds.^This channeling could be reduced by raising the superficial gas velocity to a level which, for the same particle-size distribution, depends on the density of the particles.^A good state of fluidity in a fluidized catalyst is possible except when the mean particle size is small and the size distribution is broad.^The density of the particles has a significant effect on their fluidity.^The fluidity of particles can be evaluated by plotting gas-holdup data, on the basis of recirculation theory for a bubble column.
Country of PublicationUnited States
LanguageEnglish
FormatPages: 517-526
System Entry Date2001 May 13

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