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t (s) 14 25 29 30 27 24 25 12 CAO, mol/dm³ 200 190 180 170 150 140 120 110 CA mol/dm3 100 70 20 50 40 10

t (s) 14 25 29 30 27 24 25 12 CAO, mol/dm³ 200 190 180 170 150 140 120 110 CA mol/dm3 100 70 20 50 40 10

Introduction to Chemical Engineering Thermodynamics
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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Can you show me the step how to used the formula given to get the Volume for both MFR and PFR. Just give one example from the given data. Thank you

T (s) CAO, mol/dm³ 14 25 29 30 27 24 25 12 200 190 180 170 150 140 120 110 CA, mol/dm³ 100 90 80 70 50 40 20 10 Rate, -rA, 7.142857 4 3.448276 3.333333 3.703704 4.166667 4 8.333333 mol/dm³ s V,MFR, dm³ 2380 4037.5 4437 4335 3442.5 2856 2550 1122 V, PFR, dm³ 2380 4037.5 4437 4335 3442.5 2856 2550 1122
Transcribed Image Text:T (s) CAO, mol/dm³ 14 25 29 30 27 24 25 12 200 190 180 170 150 140 120 110 CA, mol/dm³ 100 90 80 70 50 40 20 10 Rate, -rA, 7.142857 4 3.448276 3.333333 3.703704 4.166667 4 8.333333 mol/dm³ s V,MFR, dm³ 2380 4037.5 4437 4335 3442.5 2856 2550 1122 V, PFR, dm³ 2380 4037.5 4437 4335 3442.5 2856 2550 1122
a) Design equation for MFR Reactor: CAOXA CA0-CA %3D -TA -TA Design equation for PFR Reactor: =: = CA0 N dXa -C dCA CA0 -TA %3D -TA where, V=volume of reactor v=feed rate
Transcribed Image Text:a) Design equation for MFR Reactor: CAOXA CA0-CA %3D -TA -TA Design equation for PFR Reactor: =: = CA0 N dXa -C dCA CA0 -TA %3D -TA where, V=volume of reactor v=feed rate
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