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Assume the benzene (species 1) from above is part of an equimolar vapor mixture with n-hexane (species 2). Find the fugacity and fugacity coefficients at 2 bar for each species if: a.) The vapor solution forms an ideal solution. b.) The vapor solution does not form an ideal solution. c.) Can the mixture be treated as an ideal solution of vapors? Why or why not?

Assume the benzene (species 1) from above is part of an equimolar vapor mixture with n-hexane (species 2). Find the fugacity and fugacity coefficients at 2 bar for each species if: a.) The vapor solution forms an ideal solution. b.) The vapor solution does not form an ideal solution. c.) Can the mixture be treated as an ideal solution of vapors? Why or why not?

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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Assume the benzene (species 1) from above is part of an equimolar vapor
mixture with n-hexane (species 2). Find the fugacity and fugacity coefficients at 2 bar for each
species if:
a.) The vapor solution forms an ideal solution.
b.) The vapor solution does not form an ideal solution.
c.) Can the mixture be treated as an ideal solution of vapors? Why or why not?

Pressure fugacity in bar fugacity coefficient Psat=6.13762 bar 5.73 0.9336 1 bar 0.9888 0.9888 2 bar 1.9555 0.9778 12 bar 10.486 0.874
Transcribed Image Text:Pressure fugacity in bar fugacity coefficient Psat=6.13762 bar 5.73 0.9336 1 bar 0.9888 0.9888 2 bar 1.9555 0.9778 12 bar 10.486 0.874
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