What are the PFR and CSTR volumes necessary to achieve a 40% for a single reactor process?

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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100%
Problem 2
X₁0
XA
mol
dm³.min.
-TA
1 (dm³ min)
-TA mol
FAO (dm³-min
-TA
mol
1.0
0.2
1.67
0.4
5.0
0.45
5.0
0.5
5.0
0.6
= 300
5.0
Reaction ASTILBENE → BTROSPHOPHENE + CMETHANE
Feed Flow Rate
mol
sec Pure A
0.8
Adiabatic & Exothermic
1.25
0.9
0.91
Transcribed Image Text:Problem 2 X₁0 XA mol dm³.min. -TA 1 (dm³ min) -TA mol FAO (dm³-min -TA mol 1.0 0.2 1.67 0.4 5.0 0.45 5.0 0.5 5.0 0.6 = 300 5.0 Reaction ASTILBENE → BTROSPHOPHENE + CMETHANE Feed Flow Rate mol sec Pure A 0.8 Adiabatic & Exothermic 1.25 0.9 0.91
(A) What are the PFR and CSTR volumes necessary to achieve a 40% for a single reactor process?
Transcribed Image Text:(A) What are the PFR and CSTR volumes necessary to achieve a 40% for a single reactor process?
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