plz helpD What final conversion can be achieved if a 72-dm^3 PFR is followed in series by a 24-dm^3 CSTR? X₁0mol-TA dm³.min. 1.0dm³-min-TAmolFAO (dm³-min-TAmol0.21.670.45.00.455.00.5Feed Flow Rate5.00.6= 300-5.0Reaction ASTILBENE → BTROSPHOPHENE + CMETHANEmolsec PureA0.8Adiabatic & Exothermic1.250.90.91

Given, feed flow rate of ANow we tabulate data of conversion of A (XA) versus using the table…

Answered: X₁0 mol -TA dm³-min 1.0 (dm³-min) mol…

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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Question

plz helpD

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

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 (X_A) versus $fraction numerator F subscript A 0 end subscript over denominator negative r subscript A end fraction$ using the table provided.

X_A	$fraction numerator F subscript A 0 end subscript over denominator negative r subscript A end fraction$
0	300
0.2	179.6407
0.4	60
0.45	60
0.5	60
0.6	60
0.8	240
0.9	329.6703