c (C) For two CSTRS in series where each CSTR is 1.6 m^3, determine the conversion after each reactor. XA 0.0mol-TA ³-sec1 (m³-sec)-TA molFAO (m³-sec-TAmol0.490.10.410.20.340.40.199Reaction A → B0.60.117molsec PureAT = 500K & P = 830 kPa (8.2 atm)Feed Flow Rate = 0.80.70.0830.80.054

Given, feed flow rateTabulating the data of and XA…

Answered: XA 0.0 mol m³.sec. 1 m³-sec -TA -TA mol…

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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Step 1: Conversion in two CSTR in series

Given, feed flow rate

$F subscript A 0 end subscript space equals space 0.8 space fraction numerator m o l over denominator s e c end fraction$

Tabulating the data of $fraction numerator F subscript A o end subscript over denominator negative r subscript A end fraction$ and X_A

X_A	$fraction numerator F subscript A 0 end subscript over denominator negative r subscript A end fraction$	$X subscript A open parentheses fraction numerator F subscript A 0 end subscript over denominator negative r subscript A end fraction close parentheses$
0.0	1.633	0
0.1	1.951	0.1951
0.2	2.353	0.470
0.4	4.02	1.608
0.6	6.834	4.102
0.7	9.638	6.447
0.8	14.815	11.852