Reaction is Irreversible in Gas Phase in Tubular Reactor. T = Constant & Ignore Pressure Drops. Feed Volumetric Flowrate = 2400 h Concentration of Y₁ = 5.0 gmol L gmol Concentration of Y₂ = 7.0% L Concentration of Inerts = 3.0 gmol L 3Y₁ +4Y₂ → 3Y3 +4Y4 Q1) Determine the limiting reactant for the given system & reaction. Q2) Fill out table Species Y₁ Y₂ Y3 Y₁ Symbol Initial Moles gmol Fjo hour 12,000 16,800 0 0 Change Final F; Concentration C; A B C D Inert | 0 Q3) Calc the concentration of Y3 & the concentration of Y4 @ at point in reactor where conversion of the limiting reactant is 60%

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
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Reaction is Irreversible in Gas Phase in Tubular Reactor.
T = Constant & Ignore Pressure Drops.
Feed
●
Volumetric Flowrate =
Concentration of Y₁
Concentration of Y₂ =
● Concentration of Inerts
Y₁
Y₂
Y3
Y₁
=
Symbol
A
B
C
D
2400-
h
5.0 gmol
L
gmol
L
7.0%
Q1) Determine the limiting reactant for the given system & reaction.
Q2) Fill out table
Species
3Y₁ +4Y₂ → 3Y3 +4Y4
= 3.0 gmol
L
Initial Moles
gmol
Fjo
hour
12,000
16,800
0
0
Change
Final Fj
Concentration
Cj
Inert
1
0
Q3) Calc the concentration of Y3 & the concentration of Y4 @ at point in reactor where conversion of the
limiting reactant is 60%
Transcribed Image Text:Reaction is Irreversible in Gas Phase in Tubular Reactor. T = Constant & Ignore Pressure Drops. Feed ● Volumetric Flowrate = Concentration of Y₁ Concentration of Y₂ = ● Concentration of Inerts Y₁ Y₂ Y3 Y₁ = Symbol A B C D 2400- h 5.0 gmol L gmol L 7.0% Q1) Determine the limiting reactant for the given system & reaction. Q2) Fill out table Species 3Y₁ +4Y₂ → 3Y3 +4Y4 = 3.0 gmol L Initial Moles gmol Fjo hour 12,000 16,800 0 0 Change Final Fj Concentration Cj Inert 1 0 Q3) Calc the concentration of Y3 & the concentration of Y4 @ at point in reactor where conversion of the limiting reactant is 60%
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