3- For the following liquid phase parallel reaction system, A - R (desired) PR= k;Ca : k= 2 s A - S; rs= k2CA : k2= 1.5 s a-) Obtain the selectivity (Sra) expression. b-) Calculate the concentration of R at the reactor exit if the reaction is carried out in PFR and in CSTR (CAo=1 M, 9=10 L/s, overall conversion of A is 0.9) c-) Calculate the volume of PFR and CSTR reactors if the overall conversion of A is 0.9 (CAo=1 M). Note: Pure A is fed to the reactors.
3- For the following liquid phase parallel reaction system, A - R (desired) PR= k;Ca : k= 2 s A - S; rs= k2CA : k2= 1.5 s a-) Obtain the selectivity (Sra) expression. b-) Calculate the concentration of R at the reactor exit if the reaction is carried out in PFR and in CSTR (CAo=1 M, 9=10 L/s, overall conversion of A is 0.9) c-) Calculate the volume of PFR and CSTR reactors if the overall conversion of A is 0.9 (CAo=1 M). Note: Pure A is fed to the reactors.
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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Transcribed Image Text:3- For the following liquid phase parallel reaction system,
A - R (desired)
PR= k;Ca ;
k;= 2 s
A → S;
rs= k2Ca ;
k2= 1.5 s
a-) Obtain the selectivity (Sra) expression.
b-) Calculate the concentration of Rat the reactor exit if the reaction is carried out in PFR and
in CSTR (CAo=1 M, 9=10 L/s, overall conversion of A is 0.9)
c-) Calculate the volume of PFR and CSTR reactors if the overall conversion of A is 0.9 (CAo=1
М).
Note: Pure A is fed to the reactors.
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