A) Determine the reactor volumes in dm³, of a CSTR with a conversion X₁ = followed by a PFR that reaches conversion X₂ = 65% at the end of the two reactor process. = 20%
A) Determine the reactor volumes in dm³, of a CSTR with a conversion X₁ = followed by a PFR that reaches conversion X₂ = 65% at the end of the two reactor process. = 20%
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
Related questions
Question
1
![An exothermic reaction of reactant (A) forms the economically important product (B) and sellable by-
product (C),:
A-→ B+C
Which was carried out isothermally and the following data was recorded:
XA | O
mol
-TA dm3-min/ 1.2
(dm³-min)
mol
-TA
FAQ (dm³)
-TA
0.83
333.33
mol
min
0.1
1.8
0.56
222.22
0.2
1.8
0.56
0.3
3
0.33
0.5
3
= 20%
0.33
0.65
1.2
0.83
222.22 133.33 133.33 333.33
feed flow rate = 100.
pure A
A) Determine the reactor volumes in dm³, of a CSTR with a conversion
X₁
followed by a PFR that reaches conversion
X₂ 65%
at the end of the two reactor process.
1
0.8
0.75
1.33
533.33
0.95
0.5464
1.83
732.06](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fd47fc2c3-8f4b-4085-b234-bc909be774e3%2F8c04b26c-b6cb-4782-9582-95398ddc257a%2Fw61s2t_processed.png&w=3840&q=75)
Transcribed Image Text:An exothermic reaction of reactant (A) forms the economically important product (B) and sellable by-
product (C),:
A-→ B+C
Which was carried out isothermally and the following data was recorded:
XA | O
mol
-TA dm3-min/ 1.2
(dm³-min)
mol
-TA
FAQ (dm³)
-TA
0.83
333.33
mol
min
0.1
1.8
0.56
222.22
0.2
1.8
0.56
0.3
3
0.33
0.5
3
= 20%
0.33
0.65
1.2
0.83
222.22 133.33 133.33 333.33
feed flow rate = 100.
pure A
A) Determine the reactor volumes in dm³, of a CSTR with a conversion
X₁
followed by a PFR that reaches conversion
X₂ 65%
at the end of the two reactor process.
1
0.8
0.75
1.33
533.33
0.95
0.5464
1.83
732.06
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