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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 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

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
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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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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