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T isomerization of butan n-C,H10 i-C,H10 was carried out adiabatically in the liquid phase. The data for this reversible reaction are given in Table E2-5.1. (Example 11.3 shows how the data in Table E2-5.1 were generated.) TABLE E2-5.1 RAw DATA 0.0 0.2 0.4 0.6 0.65 -ra(kmol/m h) 39 53 59 38 25 X, = 0.2 X; = 0.6 Va Co X = 0.65 Figure E2-5.1 Reactors in series. Calculate the volume of each of the reactors for an entering molar flow rate of n-butane of 50 kmol/hr.

T isomerization of butan n-C,H10 i-C,H10 was carried out adiabatically in the liquid phase. The data for this reversible reaction are given in Table E2-5.1. (Example 11.3 shows how the data in Table E2-5.1 were generated.) TABLE E2-5.1 RAw DATA 0.0 0.2 0.4 0.6 0.65 -ra(kmol/m h) 39 53 59 38 25 X, = 0.2 X; = 0.6 Va Co X = 0.65 Figure E2-5.1 Reactors in series. Calculate the volume of each of the reactors for an entering molar flow rate of n-butane of 50 kmol/hr.

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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80 jo a hw 19-4_dc6c0... → →: Tisomerization of butane n-C,H10 i-C,H10 was carried out adiabatically in the liquid phase. The data for this reversible reaction are given in Table E2-5.1. (Example 11.3 shows how the data in Table E2-5.1 were generated.) TABLE E2-5.1 RAw DATA X 0.0 0.2 0.4 0.6 0.65 -r,(kmol/m h) 39 53 59 38 25 X, = 0.2 X2 = 0.6 V2 FAI X = 0.65 Figure E2-5.1 Reactors in series. Calculate the volume of each of the reactors for an entering molar flow rate of n-butane of 50 kmol/hr. Sol ically and graphically
Transcribed Image Text:80 jo a hw 19-4_dc6c0... → →: Tisomerization of butane n-C,H10 i-C,H10 was carried out adiabatically in the liquid phase. The data for this reversible reaction are given in Table E2-5.1. (Example 11.3 shows how the data in Table E2-5.1 were generated.) TABLE E2-5.1 RAw DATA X 0.0 0.2 0.4 0.6 0.65 -r,(kmol/m h) 39 53 59 38 25 X, = 0.2 X2 = 0.6 V2 FAI X = 0.65 Figure E2-5.1 Reactors in series. Calculate the volume of each of the reactors for an entering molar flow rate of n-butane of 50 kmol/hr. Sol ically and graphically
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