Max. Marks: 60 Q1 You have fixed bed reactor for the reaction [A+ B→ 2C+D], feed for the reactor 100 kmole/hr at the following condition M. wt. of A M. wt. of B M. wt. of C M. wt. of D Temp °C Press. atm. convers Density Kg/m³ ion Materi al L/D catalyst activat 150 98 87 125 45 3 79% 1100 Carbon steel 4 ed carbon Size the above reactor through calculating the following: reactor height (m), reactor dimeter(m), reactor volume(m³) and shell thickness(mm). note that (Joint Efficiency =0.7) -28.282

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
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Chapter1: Introduction
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Max. Marks: 60
Q1
You have fixed bed reactor for the reaction [A+ B→ 2C+D], feed for the reactor 100 kmole/hr at the
following condition
M. wt.
of A
M. wt.
of B
M. wt.
of C
M. wt.
of D
Temp
°C
Press.
atm.
convers Density
Kg/m³
ion
Materi
al
L/D
catalyst
activat
150
98
87
125
45
3
79%
1100
Carbon
steel
4
ed
carbon
Size the above reactor through calculating the following: reactor height (m), reactor dimeter(m), reactor
volume(m³) and shell thickness(mm). note that (Joint Efficiency =0.7)
-28.282
Transcribed Image Text:Max. Marks: 60 Q1 You have fixed bed reactor for the reaction [A+ B→ 2C+D], feed for the reactor 100 kmole/hr at the following condition M. wt. of A M. wt. of B M. wt. of C M. wt. of D Temp °C Press. atm. convers Density Kg/m³ ion Materi al L/D catalyst activat 150 98 87 125 45 3 79% 1100 Carbon steel 4 ed carbon Size the above reactor through calculating the following: reactor height (m), reactor dimeter(m), reactor volume(m³) and shell thickness(mm). note that (Joint Efficiency =0.7) -28.282
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