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: McGraw-Hill Education
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Chapter 10, Problem 10.32P
Interpretation Introduction

Interpretation:

We have to prove excess properties of binary gas mixtures in given terms.

Concept introduction:

The gas mixture fugacity coefficients are partial molar properties of the excess Gibbs free energy, hence partial molar properties of the total fugacity can be written as follows:

  lnϕ=[( G E /RT)ni]P,T,nj

Excess properties are the difference between real gas property to ideal gas property.

Equation (3.36) and (10.62) mentioned in question are:

  Z=1+BPRTB=ij y i y j B i,j

All excess properties in terms of excess Gibbs free energy given in Table 10.1 in the book are:

  VE=( ( GE ) P)T,ySE=( ( GE ) T)P,yHE=GE+TSEHE=GE+T[( ( G E ) T )P,y]HE=RT2( ( GE/RT ) T)P,yCPE=( H E T)P,yCPE=T( 2 G E T 2 )P,y

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