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Modern Engineering Thermodynamics

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

Table 12.1 summarizes the four composition measures thus far defined.<br />

Dividing both sides of Eq. (12.5) by the mixture mass m m produces the specific volume of the mixture as<br />

v m = V m<br />

m m<br />

= ∑ N<br />

i=1<br />

m i<br />

m m<br />

^v i = ∑w i^v i<br />

where w i is the mass fraction m i /m m . The concepts of total, specific, and partial specific properties can<br />

be extended to other extensive properties, as shown in Table 12.2. On a molar basis, total, molar specific, and<br />

partial molar specific properties are defined in Table 12.3.<br />

Finally, the constant volume and constant pressure specific heats for the mixture are defined as<br />

<br />

c vm = ∂u <br />

<br />

m<br />

and c pm = ∂h <br />

m<br />

∂T m v m<br />

∂T m<br />

These specific heats can also be written on a molar basis and in terms of the partial specific heats of the component<br />

gases, as shown in Table 12.4.<br />

The mass, mole, volume, and pressure composition fractions have the characteristic that they always sum to<br />

unity; that is,<br />

v m<br />

∑ N<br />

w i = ∑ N<br />

χ i = ∑ N<br />

Ψ i = ∑ N<br />

π i = 1:0 (12.10)<br />

i=1 i=1 i=1 i=1<br />

Table 12.1 Four Composition Measures<br />

Name of Composition Fraction<br />

Defining Equation<br />

Mass fraction w i<br />

Mole fraction χ i<br />

Volume fraction ψ i<br />

Partial pressure fraction π i<br />

w i = m i /m m<br />

χ i<br />

= n i /n m<br />

ψ i = V i / V m<br />

π i = p i /p m<br />

Table 12.2 Total, Specific, and Partial Specific Properties of a Mixture of Gases<br />

Total Property of the Mixture<br />

V m = ∑ N<br />

m i^v i<br />

i=1<br />

U m = ∑ N<br />

m i^u i<br />

i=1<br />

H m = ∑ N<br />

m i^hi<br />

i=1<br />

S m = ∑ N<br />

m i^s i<br />

i=1<br />

Partial Specific Property<br />

Specific Property of the Mixture of Gas i in the Mixture<br />

<br />

v m = V m /m m = ∑ N<br />

mi ^v i = ∑ N<br />

w<br />

^v<br />

mm i^v i = ∂V <br />

m<br />

i ∂m i pm,Tm,mj<br />

i=1 i=1<br />

<br />

u m = U m /m m = ∑ N<br />

mi ^u i = ∑ N<br />

w<br />

^u<br />

mm i^u i = ∂U <br />

m<br />

i ∂m i pm,Tm,mj<br />

i=1<br />

i=1<br />

<br />

h m = H m /m m = ∑ N<br />

mi ^h<br />

mm i = ∑ N<br />

^hi<br />

w<br />

= ∂H <br />

m<br />

i^hi ∂m i pm,Tm,mj<br />

i=1<br />

i=1<br />

<br />

s m = S m /m m = ∑ N<br />

mi ^s i = ∑ N<br />

w<br />

^s<br />

mm i^s i = ∂S <br />

m<br />

i ∂m i<br />

i=1<br />

i=1<br />

pm,Tm,mj<br />

CRITICAL THINKING<br />

Is it possible to define a partial temperature of gas i in a mixture of N gases? Since the mixture temperature varies inversely<br />

with the system mass in most equations of state for gases, is temperature a homogeneous function of the first degree in the<br />

masses m i ? Could the partial temperature of gas i in the mixture be the temperature exhibited by gas i when it alone occupies<br />

the volume of the mixture Vm at the pressure of the mixture p m ? (See Problem 67 at the end of this chapter.)

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