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Modern Engineering Thermodynamics

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

where the mixture specific heats are given by<br />

c vm<br />

= ∑ N<br />

i=1<br />

w i^c vi and c pm = ∑ N<br />

6. The study of the special mixture of ideal gases of dry air and water vapor is called psychrometrics, and the two<br />

important composition measures used in the field of meteorology are<br />

a. The relative humidity ϕ of the mixture, defined as<br />

ϕ = p w<br />

p sat<br />

where p w is the actual partial pressure of the water vapor in the mixture and p sat is the saturation pressure<br />

of the water vapor at the temperature of the mixture.<br />

b. The humidity ratio ω of the mixture, defined as<br />

ω = m w<br />

m a<br />

where m w is the mass of water vapor present in the mixture and m a is the mass of dry air present in the<br />

mixture. These two composition measures are related by<br />

<br />

ϕp sat<br />

ω = 0:622<br />

p m − ϕp sat<br />

7. The dew point temperature T DP is defined as<br />

T DP = T sat ðevaluated at p w Þ<br />

where p w is the partial pressure of the water vapor present, p w = ϕp sat .<br />

8. The humidity ratio at the inlet to an adiabatic saturator is given by<br />

ω 1 = c paðT 2 − T 1 Þ + ω 3 ðh fg2 Þ<br />

h g1 − h f 2<br />

9. The psychrometric enthalpy h # of the mixture is defined as<br />

i=1<br />

w i^c pi<br />

10. For mixtures of real gases, we can use<br />

a. The Dalton compressibility factor, Z Dm ,<br />

where<br />

h # = H m<br />

m a<br />

= h a + ωh w<br />

p m V m = Z Dm m m R m T m<br />

b. the Amagat compressibility factor, Z Am ,<br />

where<br />

Z Dm = ∑ N<br />

i=1<br />

<br />

w i M m<br />

Z Di = ∑ N<br />

χ<br />

M i Z Di<br />

i<br />

i=1<br />

p m V Am = Z Am m m R m T m<br />

c. the Kay compressibility factor, Z Km ,<br />

Z Am = ∑ N<br />

ðw i M m /M i ÞZ Ai = ∑ N<br />

x i Z Ai<br />

i=1<br />

i=1<br />

p m Vm = Z Km m m R m T m<br />

where Z Km is found from the pseudocritical pressure and temperature of the mixture<br />

p cm = ∑ N<br />

x i p ci and T cm = ∑ N<br />

x i T ci<br />

i=1<br />

i=1

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