A liquid-phase reaction with final conversion X = 0.7 is going to be carried out in a series of CSTR and PFR reactors to produce an anticancer drug. The Levenspiel plot for the data gathered in batch reactor is given below.

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
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2- Question 2:
A liquid-phase reaction with final conversion X = 0.7 is going to be carried out in a series of CSTR
and PFR reactors to produce an anticancer drug. The Levenspiel plot for the data gathered in batch
reactor is given below.
60
50
40
FAO
(m²)
TA
30
20
10
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
Conversion X
b) What would be your best reactor series and total volume for this conversion?
a) O One CSTR. V= 21 m³ up to X = 0.7
b) O Two CSTR. V = 1 m³ up to X = 0.3 and V2 = 10 m3 up to X = 0.7
%3D
c) One PFR. V= 18.9 m³ up to X = 0.7
d)
Two PFR. V, = 6 m up to X = 0.3 and V2 = 12.9 m² up to X = 0.7
e) Two CSTR. V, = 3 m² up to X = 0.3 and V2 = 12 m³ up to X = 0.7
Leave blank
Transcribed Image Text:2- Question 2: A liquid-phase reaction with final conversion X = 0.7 is going to be carried out in a series of CSTR and PFR reactors to produce an anticancer drug. The Levenspiel plot for the data gathered in batch reactor is given below. 60 50 40 FAO (m²) TA 30 20 10 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 Conversion X b) What would be your best reactor series and total volume for this conversion? a) O One CSTR. V= 21 m³ up to X = 0.7 b) O Two CSTR. V = 1 m³ up to X = 0.3 and V2 = 10 m3 up to X = 0.7 %3D c) One PFR. V= 18.9 m³ up to X = 0.7 d) Two PFR. V, = 6 m up to X = 0.3 and V2 = 12.9 m² up to X = 0.7 e) Two CSTR. V, = 3 m² up to X = 0.3 and V2 = 12 m³ up to X = 0.7 Leave blank
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