ELEMENTARY PRINCIPLES OF CHEM. PROCESS.
ELEMENTARY PRINCIPLES OF CHEM. PROCESS.
4th Edition
ISBN: 9781119249214
Author: FELDER
Publisher: INTER WILE
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Chapter 2, Problem 2.3P
Interpretation Introduction

Interpretation:

To estimate number of baseballs to be placed in classroom.

Concept introduction:

The classroom is in the form of a rectangle and the volume of rectangle is defined as the product of length, breadth and height.

V=l×b×h

Here, V is the volume of classroom, l is the length of the classroom, b is the breadth of the classroom and h is height of the classroom.

The unit of volume is cubic meter.

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An 8-foot ion exchange bed needs to be backwashed with water to remove impurities. The particles have a density of 1.24 g/cm³ and an average size of 1.1 mm.   Calculate:   a. The minimum fluidization velocity using water at 30°C?   b. The velocity required to expand the bed by 30%?   Assumptions: The ion exchange bed particles are spherical (sphericity = 1.1), and the minimum fluidization porosity (ɛM) is 0.3.   Notes: At 30°C, the viscosity (μ) of water is 0.797 cP, and the density (ρ) is 0.995 g/cm³.
fluidized bed reactor uses a solid catalyst with a particle diameter of 0.25 mm, a bulk density of 1.50 g/mL, and a sphericity of 0.90. Under packed bed conditions, the porosity is 0.35, and the bed height is 2 m. The gas enters from the bottom of the reactor at a temperature of 600°C, with a viscosity of 0.025 cP and a density of 0.22 lb/ft³. At minimum fluidization, the porosity reaches 0.45. Calculate: a. The minimum superficial velocity (VM) of the gas entering the fluidized column. b. The bed height if V = 2 VM c. The pressure drop under conditions where V =2.5 VM
A fluidized bed reactor uses a solid catalyst with a particle diameter of 0.25 mm, a bulk density of 1.50 g/mL, and a sphericity of 0.90. Under packed bed conditions, the porosity is 0.35, and the bed height is 2 m. The gas enters from the bottom of the reactor at a temperature of 600°C, with a viscosity of 0.025 cP and a density of 0.22 lb/ft³. At minimum fluidization, the porosity reaches 0.45.   Calculate:   a. The minimum superficial velocity (VM) of the gas entering the fluidized column.   b. The bed height if V = 2 VM   c. The pressure drop under conditions where V =2.5 VM
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