X₁0 mol -TA dm³-min 1.0 (dm³-min) mol -TA FAO (dm³-min) -TA mol 0.2 1.67 0.4 5.0 0.45 5.0 0.5 5.0 0.6 5.0 Feed Flow Rate = 300- mol sec Pure A Reaction ASTILBene → BTROSPHOPHENE + CMETHANE 0.8 Adiabatic & Exothermic 1.25 0.9 0.91

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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What final conversion can be achieved if a 72-dm^3 PFR is followed in series by a 24-dm^3 CSTR?
Transcribed Image Text:What final conversion can be achieved if a 72-dm^3 PFR is followed in series by a 24-dm^3 CSTR?
X₁0
mol
-TA dm³.min. 1.0
dm³-min
-TA
mol
FAO (dm³-min
-TA
mol
0.2
1.67
0.4
5.0
0.45
5.0
0.5
Feed Flow Rate
5.0
0.6
= 300-
5.0
Reaction ASTILBENE → BTROSPHOPHENE + CMETHANE
mol
sec PureA
0.8
Adiabatic & Exothermic
1.25
0.9
0.91
Transcribed Image Text:X₁0 mol -TA dm³.min. 1.0 dm³-min -TA mol FAO (dm³-min -TA mol 0.2 1.67 0.4 5.0 0.45 5.0 0.5 Feed Flow Rate 5.0 0.6 = 300- 5.0 Reaction ASTILBENE → BTROSPHOPHENE + CMETHANE mol sec PureA 0.8 Adiabatic & Exothermic 1.25 0.9 0.91
Expert Solution
Step 1: Conversion in PFR followed by CSTR

Given, feed flow rate of A

F subscript A 0 end subscript space equals space 300 space fraction numerator m o l over denominator s e c end fraction

Now we tabulate data of conversion of A (XA) versus fraction numerator F subscript A 0 end subscript over denominator negative r subscript A end fraction using the table provided. 

XAfraction numerator F subscript A 0 end subscript over denominator negative r subscript A end fraction
0300
0.2179.6407
0.460
0.4560
0.560
0.660
0.8240
0.9329.6703

Now we will plot curve between XA and FA0/-rA using Microsoft Excel. 

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