Calculate the velocity of fluidization, uo, of a catalytic bed of diameter D = 2 f and initial height ho= 3 ft. The bed is packed with solid particles of density p 2g/cm3 and mean diameter Dp= 0.5 cm, under continuous flow of fluid o viscosity u,= 1 cP and density P;= 1g/cm³. What power input is required a luidization? [Assume that the catalytic reactor is packed in a cubi arrangement, ɛ = 1 – ]. -

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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Calculate the velocity of fluidization, uo, of a catalytic bed of diameter D = 2 ft
and initial height ho= 3 ft. The bed is packed with solid particles of density p=
%3D
2g/cm3 and mean diameter Dp= 0.5 cm, under continuous flow of fluid of
viscosity u,= 1 cP and density P;= 1g/cm3. What power input is required at
fluidization? [Assume that the catalytic reactor is packed in a cubic
arrangement, E = 1 – ].
Transcribed Image Text:Calculate the velocity of fluidization, uo, of a catalytic bed of diameter D = 2 ft and initial height ho= 3 ft. The bed is packed with solid particles of density p= %3D 2g/cm3 and mean diameter Dp= 0.5 cm, under continuous flow of fluid of viscosity u,= 1 cP and density P;= 1g/cm3. What power input is required at fluidization? [Assume that the catalytic reactor is packed in a cubic arrangement, E = 1 – ].
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