Unit Operations of Chemical Engineering
Unit Operations of Chemical Engineering
7th Edition
ISBN: 9780072848236
Author: Warren McCabe, Julian C. Smith, Peter Harriott
Publisher: McGraw-Hill Companies, The
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Chapter 7, Problem 7.11P
Interpretation Introduction

Interpretation: The diameter of the vessel which just fluidize the catalyst at the given conditions is to be calculated.

Concept introduction: The condition at which particles just fluidize is called minimum fluidized condition and the expression for same is,

  ΔPL=g(1-εM)(ρp-ρ).......(1)

In the above formula, the notations used are,

  ΔP=PressuredropthroughvesselL=LengthofthevesselεM=MinimumBedporosityρp=Densityofparticlesρ=Densityofairg=Accelerationduetogravity

The Ergun equation for the particles is given as,

  ΔPL=150V¯0μ(1-ε)2ϕs2Dp2ε3+1.75V¯02ρ(1-ε)ϕsDpε3 ……. (2)

  ΔP=PressuredropthroughvesselL=LengthofvesselV¯0=Superficialvelocityμ=Viscosityoffluidε=BedporosityDp=Pelletdiameterϕs=Sphericityofparticles

  ρ=Densityofair

The density of air can be given as,

  ρ=PMRT.......(3)

In the equation (3), notations used are,

P is the pressure at which air enters

M is the molecular weight of air

R is the Universal Gas constant

T is the temperature at which air enters

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(11.35. For a binary gas mixture described by Eqs. (3.37) and (11.58), prove that: 4812 Pу132 ✓ GE = 812 Py1 y2. ✓ SE dT HE-12 T L = = (812 - 7 1/8/123) d² 812 Pylyz C=-T Pylyz dT dT² See also Eq. (11.84), and note that 812 = 2B12 B11 - B22. perimental values of HE for binary liquid mixtures of
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Unit Operations of Chemical Engineering
Chemical Engineering
ISBN:9780072848236
Author:Warren McCabe, Julian C. Smith, Peter Harriott
Publisher:McGraw-Hill Companies, The