Desired (D) and undesirable (U) substances are produced in the reactions that take place in the liquid phase. Which of the following reactor(s) should be preferred to increase the required (D) substance production? Why is that? Could you have a different reactor design for high volume D production?
Desired (D) and undesirable (U) substances are produced in the reactions that take place in the liquid phase. Which of the following reactor(s) should be preferred to increase the required (D) substance production? Why is that? Could you have a different reactor design for high volume D production?
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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Question
Desired (D) and undesirable (U) substances are produced in the reactions that take place in the liquid phase. Which of the following reactor(s) should be preferred to increase the required (D) substance production? Why is that? Could you have a different reactor design for high volume D production?
Answer separately for the following three different situations.
![I. situation
k
A+B-
5 =k,(C'(C,)?
Еa 3 27.5 kJ/mol
A+B-
k
→U
Еa 3 37.5 k.J/mol
II. situation
A+B-
5=k,(C,J°(C, )?
→D
Ea = 42.5 kJ/mol
k
A+B-K »U
Еa%3D27,5 kJ/mol
III. situation
A+B-
→D
Ea = 32.5 kJ/mol
k
A+B
, =k,(C,)'(C,)'
Еa%3D14.8 kJ/mol
B
(a) PFR
(b) PFR
(c) CSTR
t-0
A
B
(d) Semibatch
(e) Batch
() Semibatch
-B
(g)](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fc70dd208-86af-491e-9169-a064ea87ce01%2F6952e8c6-72fb-47de-8ea8-65631858953f%2F3mnlroq_processed.png&w=3840&q=75)
Transcribed Image Text:I. situation
k
A+B-
5 =k,(C'(C,)?
Еa 3 27.5 kJ/mol
A+B-
k
→U
Еa 3 37.5 k.J/mol
II. situation
A+B-
5=k,(C,J°(C, )?
→D
Ea = 42.5 kJ/mol
k
A+B-K »U
Еa%3D27,5 kJ/mol
III. situation
A+B-
→D
Ea = 32.5 kJ/mol
k
A+B
, =k,(C,)'(C,)'
Еa%3D14.8 kJ/mol
B
(a) PFR
(b) PFR
(c) CSTR
t-0
A
B
(d) Semibatch
(e) Batch
() Semibatch
-B
(g)
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