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Modern Engineering Thermodynamics

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414 CHAPTER 12: Mixtures of Gases and Vapors<br />

Finally, the thermodynamic description of a mixture of ideal gases was completed through the work of Josiah<br />

Willard Gibbs (1838–1903), who generalized Dalton’s law to define all the partial properties (except volume) of<br />

the components in the mixture to be equal to the values that those properties would have if each component<br />

gas alone occupied the volume of the mixture at the temperature of the mixture and at the partial pressure of<br />

that component. The Gibbs-Dalton ideal gas mixture law presumesthatnomolecularinteractionstakeplace<br />

between the components of the mixture, because each component is presumed to behave as though the other<br />

components were not present.<br />

Undertheseconditions,weconcludethatalltheextensiveproperties of a mixture of ideal gases are conserved, and the<br />

mixture value of any extensive property can be determined by summing the contributions made by each gas present in the<br />

mixture.<br />

Therefore, for ideal gases only,<br />

V m = ∑ N<br />

i=1<br />

V i<br />

= ∑ N<br />

and the specific volume of this mixture can be calculated from<br />

v m = V m<br />

m m<br />

= ∑ N<br />

i=1<br />

i=1<br />

m i v i (12.21)<br />

m i<br />

v i = ∑ N<br />

w i v i (12.22)<br />

m m<br />

where w i is the mass fraction of ideal gas i in the mixture and v i is the specific volume of that gas determined at<br />

thepressureandtemperatureofthemixture(i.e.,v i = R i T m /p m ). Table 12.5 lists the mass and molar equations<br />

for all the total and specific properties of a mixture of ideal gases.<br />

The mass fraction w i ,themolefractionχ i ,thevolumefractionψ i, and the pressure fraction π i make four<br />

composition measures that can be used to describe a mixture. However, for ideal gases, there is a simple<br />

relation between these four quantities. From Eqs. (12.16) and (12.18), we can write the pressure and volume<br />

fractions as<br />

and<br />

i=1<br />

π i = p i<br />

=<br />

m iR i T m /V m<br />

= w iR i<br />

= w iM m<br />

= n i<br />

= χ<br />

p m m m R m T m /V m R m M i n i<br />

m<br />

ψ i = V i<br />

=<br />

m iR i T m /p m<br />

= w iR i<br />

V m m m R m T m /p m R m<br />

= w iM m<br />

M i<br />

= n i<br />

n m<br />

= χ i<br />

Table 12.5 Mass and Molar Total and Specific Thermodynamic Properties of Ideal<br />

Gas Mixtures<br />

Total Property Mass Specific Property Molar Specific Property<br />

V m = ∑ N<br />

V i<br />

= ∑ N<br />

m i v i<br />

i=1 i=1<br />

U m = ∑ N<br />

U i = ∑ N<br />

m i u i<br />

i=1 i=1<br />

H m = ∑ N<br />

H i = ∑ N<br />

m i h i<br />

i=1 i=1<br />

S m = ∑ N<br />

S i = ∑ N<br />

m i s i<br />

i=1 i=1<br />

v m = ∑ N<br />

w i v i<br />

i=1<br />

u m = ∑ N<br />

w i u i<br />

i=1<br />

h m = ∑ N<br />

w i h i<br />

i=1<br />

s m = ∑ N<br />

w i s i<br />

i=1<br />

c vm = ∑ N<br />

w i c vi<br />

i=1<br />

c pm = ∑ N<br />

w i c pi<br />

i=1<br />

v m = ∑ N<br />

χ i v i<br />

i=1<br />

u m = ∑ N<br />

χ i u i<br />

i=1<br />

h m = ∑ N<br />

χ i h i<br />

i=1<br />

s m = ∑ N<br />

χ i s i<br />

i=1<br />

c vm = ∑ N<br />

χ i c vi<br />

i=1<br />

c pm = ∑ N<br />

χ i c pi<br />

i=1

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