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B The isomerization of butane C,H10 -C,H was carried out in the liquid phase. The data for this reversible reaction are given in Table below. 0.0 02 0.4 0.6 0.65 A (kmolim'.h) 39 53 38 25 59 This reaction has been done in three different reactors as shown below: X- 0.1 X= 0.5 Xạ 0.6 Calculate the volume of cach of the reactors for an entering molar flow rate of n-butane of 52 kmol/hr.

B The isomerization of butane C,H10 -C,H was carried out in the liquid phase. The data for this reversible reaction are given in Table below. 0.0 02 0.4 0.6 0.65 A (kmolim'.h) 39 53 38 25 59 This reaction has been done in three different reactors as shown below: X- 0.1 X= 0.5 Xạ 0.6 Calculate the volume of cach of the reactors for an entering molar flow rate of n-butane of 52 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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B- The isomerization of butane C,H10-C,H0 was carried out in the liquid phase. The data for this reversible reaction are given in Table below. 0.0 0.2 0.4 0.6 0.65 A (kmol/m'.h) This reaction has been done in three different reactors as shown below: 39 53 59 38 25 X;= 0.1 X 0.5 X- 0.6 Calculate the volume of cach of the reactors for an entering molar flow rate of n-butane of 52 kmol/hr.
Transcribed Image Text:B- The isomerization of butane C,H10-C,H0 was carried out in the liquid phase. The data for this reversible reaction are given in Table below. 0.0 0.2 0.4 0.6 0.65 A (kmol/m'.h) This reaction has been done in three different reactors as shown below: 39 53 59 38 25 X;= 0.1 X 0.5 X- 0.6 Calculate the volume of cach of the reactors for an entering molar flow rate of n-butane of 52 kmol/hr.
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