0.02 m and length equal to the diameter. The density of the catalyst is 1600 kg/m³ and the A packed bed is composed of catalyst particles in the form of cylinders having a diameter of porosity is 0.399 a) Calculate the sphericity of the catalyst particles b) Calculate the effective diameter of the catalyst particles (deff=dsph) c) If the gas flow rate through the catalyst bed is 0.70 kg/m²s, calculate the pressure drop across the bed assuming that the gas enters at atmospheric pressure Viscosity of the gas = 0.04 Ns/m² Average temperature of the gas 650 K The composition of the fluid is given in Table 1 mol % MM Component Inlet Outlet g/mol A 20 9 27 B 52 63 42 C 28 28 61 Table 1: Gas composition of inlet and outlet gas
0.02 m and length equal to the diameter. The density of the catalyst is 1600 kg/m³ and the A packed bed is composed of catalyst particles in the form of cylinders having a diameter of porosity is 0.399 a) Calculate the sphericity of the catalyst particles b) Calculate the effective diameter of the catalyst particles (deff=dsph) c) If the gas flow rate through the catalyst bed is 0.70 kg/m²s, calculate the pressure drop across the bed assuming that the gas enters at atmospheric pressure Viscosity of the gas = 0.04 Ns/m² Average temperature of the gas 650 K The composition of the fluid is given in Table 1 mol % MM Component Inlet Outlet g/mol A 20 9 27 B 52 63 42 C 28 28 61 Table 1: Gas composition of inlet and outlet gas
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:0.02 m and length equal to the diameter. The density of the catalyst is 1600 kg/m³ and the
A packed bed is composed of catalyst particles in the form of cylinders having a diameter of
porosity is 0.399
a) Calculate the sphericity of the catalyst particles
b) Calculate the effective diameter of the catalyst particles (deff=dsph)
c) If the gas flow rate through the catalyst bed is 0.70 kg/m²s, calculate the pressure drop
across the bed assuming that the gas enters at atmospheric pressure
Viscosity of the gas = 0.04 Ns/m²
Average temperature of the gas 650 K
The composition of the fluid is given in Table 1
mol %
MM
Component
Inlet
Outlet
g/mol
A
20
9
27
B
52
63
42
C
28
28
61
Table 1: Gas composition of inlet and outlet gas
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