1. What PFR volume is necessary to achieve 50% conversion? 2. What CSTR volume is necessary to achieve 50% conversion? 3. What is the volume of a second CSTR added in series to the first CSTR (Part b) necessary to achieve an overall conversion of 80%? (Ans: VCSTR = 1.5x105 m³)

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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Plz answer what u can it is a multi-part question, i will answer what i can. 

Figure P2-7B Levenspiel plot.
1. What PFR volume is necessary to achieve 50% conversion?
2. What CSTR volume is necessary to achieve 50% conversion?
3. What is the volume of a second CSTR added in series to the first CSTR
(Part b) necessary to achieve an overall conversion of 80%? (Ans:
VCSTR = 1.5 × 105 m³)
4. What PFR volume must be added to the first CSTR (Part b) to raise the
conversion to 80%?
5. What conversion can be achieved in a 6 × 104 m³ CSTR? In a 6 × 104
3
3
m PFR?
Transcribed Image Text:Figure P2-7B Levenspiel plot. 1. What PFR volume is necessary to achieve 50% conversion? 2. What CSTR volume is necessary to achieve 50% conversion? 3. What is the volume of a second CSTR added in series to the first CSTR (Part b) necessary to achieve an overall conversion of 80%? (Ans: VCSTR = 1.5 × 105 m³) 4. What PFR volume must be added to the first CSTR (Part b) to raise the conversion to 80%? 5. What conversion can be achieved in a 6 × 104 m³ CSTR? In a 6 × 104 3 3 m PFR?
P2-7B OEQ
irreversible gas-phase reaction
FAQ (m³)
-TA
is to be carried out in a flow reactor for an equimolar feed of A
and B. A Levenspiel plot for this reaction is shown in Figure
P2-7B-
500,000
400,000
300,000
200,000
The adiabatic exothermic
100,000
2A + B → 2C
0.3
X
Figure P2-7B Levenspiel plot.
0.6
0.9
Transcribed Image Text:P2-7B OEQ irreversible gas-phase reaction FAQ (m³) -TA is to be carried out in a flow reactor for an equimolar feed of A and B. A Levenspiel plot for this reaction is shown in Figure P2-7B- 500,000 400,000 300,000 200,000 The adiabatic exothermic 100,000 2A + B → 2C 0.3 X Figure P2-7B Levenspiel plot. 0.6 0.9
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