Calculate the velocity of fluidization of a catalytic bed of diameter D = 2ft and initial height Ho= 3ft. The bed is packed with solid particles of density ps = 2 g/cm³and effective diameter Dp = 0.5cm, under continuous flow of fluid of viscosity µ = 1cP and density på = 1 g/cm³. The void fraction, ɛ, equals ɛ = 1- n/6 (cubic arrangement of particles). What power input is required at fluidization? %3D
Calculate the velocity of fluidization of a catalytic bed of diameter D = 2ft and initial height Ho= 3ft. The bed is packed with solid particles of density ps = 2 g/cm³and effective diameter Dp = 0.5cm, under continuous flow of fluid of viscosity µ = 1cP and density på = 1 g/cm³. The void fraction, ɛ, equals ɛ = 1- n/6 (cubic arrangement of particles). What power input is required at fluidization? %3D
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
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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Transcribed Image Text:Calculate the velocity of fluidization of a catalytic bed of diameter D = 2ft and
initial height Ho= 3ft. The bed is packed with solid particles of density p, =
2 g/cm³and effective diameter Dp = 0.5cm, under continuous flow of fluid of
viscosity µ = 1cP and density på = 1 g/cm³. The void fraction, ɛ, equals ɛ =
1- n/6 (cubic arrangement of particles). What power input is required at
fluidization?
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