A mixture of 2 moles propane (1), 3 moles butane (2), and 5 moles pentane (3) is contained at 30 bar and 200°C. The van der Waals constants for these species are: Species a JM³ mol Propane Butane Pentane 0.94 1.45 1.91 b JM³ mol -2 9.06 × 10-5 1.22 × 10-4 -4 1.45 x 101 Determine the fugacity and fugacity coefficient of propane using the following approximations: (a) the Lewis fugacity rule

Introduction to Chemical Engineering Thermodynamics
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Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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Chapter1: Introduction
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A mixture of 2 moles propane (1), 3 moles butane (2), and 5 moles pentane (3) is contained at 30 bar and 200°C. The van der
Waals constants for these species are:
Species a JM³mol−²
b JM³mol−²
Propane
Butane
Pentane
0.94
1.45
1.91
-5
9.06 × 107
-4
1.22 × 107
-4
1.45 × 107
Determine the fugacity and fugacity coefficient of propane using the following approximations:
(a) the Lewis fugacity rule
Transcribed Image Text:A mixture of 2 moles propane (1), 3 moles butane (2), and 5 moles pentane (3) is contained at 30 bar and 200°C. The van der Waals constants for these species are: Species a JM³mol−² b JM³mol−² Propane Butane Pentane 0.94 1.45 1.91 -5 9.06 × 107 -4 1.22 × 107 -4 1.45 × 107 Determine the fugacity and fugacity coefficient of propane using the following approximations: (a) the Lewis fugacity rule
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