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Handbook of air conditioning and refrigeration / Shan K

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Moist Volume<br />

where h a <strong>and</strong> H w are, respectively, enthalpy <strong>of</strong> dry <strong>air</strong> <strong>and</strong> total enthalpy <strong>of</strong> water vapor, in Btu/lb<br />

(kJ/kg). The following assumptions are made for the enthalpy calculations <strong>of</strong> moist <strong>air</strong>:<br />

1. The ideal gas equation <strong>and</strong> the Gibbs-Dalton law are valid.<br />

2. The enthalpy <strong>of</strong> dry <strong>air</strong> is equal to zero at 0°F (�17.8°C).<br />

3. All water vapor contained in the moist <strong>air</strong> is vaporized at 0°F (�17.8°C).<br />

4. The enthalpy <strong>of</strong> saturated water vapor at 0°F (�17.8°C) is 1061 Btu/lb (2468 kJ/kg).<br />

5. For convenience in calculation, the enthalpy <strong>of</strong> moist <strong>air</strong> is taken to be equal to the enthalpy <strong>of</strong> a mixture<br />

<strong>of</strong> dry <strong>air</strong> <strong>and</strong> water vapor in which the amount <strong>of</strong> dry <strong>air</strong> is exactly equal to 1 lb (0.454 kg).<br />

Based on the preceeding assumptions, the enthalpy h <strong>of</strong> moist <strong>air</strong> can be calculated as<br />

h � ha � whw (2.26)<br />

where hw � specific enthalpy <strong>of</strong> water vapor, Btu/lb (kJ/kg). In a temperature range <strong>of</strong> 0 to 100°F<br />

(�17.8 to 37.8°C), the mean value for the specific heat <strong>of</strong> dry <strong>air</strong> can be taken as 0.240 Btu/lb�°F<br />

(1.005 kJ/kg�K). Then the specific enthalpy <strong>of</strong> dry <strong>air</strong> ha is given by<br />

h a � c pd T � 0.240 T (2.27)<br />

where c pd � specific heat <strong>of</strong> dry <strong>air</strong> at constant pressure, Btu/lb�°F (kJ/kg�K)<br />

T � temperature <strong>of</strong> dry <strong>air</strong>, °F (°C)<br />

The specific enthalpy <strong>of</strong> water vapor h w at constant pressure can be approximated as<br />

h w � h g0 � c psT (2.28)<br />

where h g0 � specific enthalpy <strong>of</strong> saturated water vapor at 0°F (�17.8°C)—its value can be taken<br />

as 1061 Btu/lb (2468 kJ/kg)<br />

c ps � specific heat <strong>of</strong> water vapor at constant pressure, Btu/lb�°F (kJ/kg�K)<br />

In a temperature range <strong>of</strong> 0 to 100°F (�17.8 to 37.8°C), its value can be taken as 0.444 Btu/lb�°F<br />

(1.859 kJ/kg�K). Then the enthalpy <strong>of</strong> moist <strong>air</strong> can be evaluated as<br />

h � c pdT � w(h g0 � c psT) � 0.240 T � w(1061 � 0.444 T) (2.29)<br />

Here, the unit <strong>of</strong> h is Btu/lb <strong>of</strong> dry <strong>air</strong> (kJ/kg <strong>of</strong> dry <strong>air</strong>). For simplicity, it is <strong>of</strong>ten expressed as<br />

Btu/lb (kJ/kg).<br />

The moist volume <strong>of</strong> moist <strong>air</strong> v, ft 3 /lb (m 3 /kg), is defined as the volume <strong>of</strong> the mixture <strong>of</strong> the dry<br />

<strong>air</strong> <strong>and</strong> water vapor when the mass <strong>of</strong> the dry <strong>air</strong> is exactly equal to 1 lb (1 kg), that is,<br />

where V � total volume <strong>of</strong> mixture, ft 3 (m 3 )<br />

m a � mass <strong>of</strong> dry <strong>air</strong>, lb (kg)<br />

(2.30)<br />

In a moist <strong>air</strong> sample, the dry <strong>air</strong>, water vapor, <strong>and</strong> moist <strong>air</strong> occupy the same volume. If we apply<br />

the ideal gas equation, then<br />

v � V<br />

m a<br />

v � V<br />

m a<br />

� R aT R<br />

p at � p w<br />

PSYCHROMETRICS 2.9<br />

(2.31)

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