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Handbook of air conditioning and refrigeration / Shan K

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(T w2 � T w1)/(h s � h a), or their average, 1/2[1/(h s86 � h a78) � 1/(h s85 � h a78)]. The tower coefficient<br />

<strong>of</strong> the cooling tower that cools the condenser water from 95 to 85°F is the summation or<br />

integration <strong>of</strong> the tower coefficient <strong>of</strong> 95 to 94°F,...,86 to 85°F.<br />

From App. Table B.1, at a wet-bulb temperature <strong>of</strong> 78°F, the enthalpy <strong>of</strong> saturated <strong>air</strong> is 41.59<br />

Btu/lb. Because the enthalpy <strong>of</strong> the saturated <strong>air</strong> film at a water temperature 85°F is 49.45 Btu/lb,<br />

the enthalpy difference between the saturated <strong>air</strong> film at 85°F <strong>and</strong> <strong>air</strong> at 78°F wet-bulb temperature<br />

is h s � h a � 49.45 � 41.59 � 7.86 Btu/lb, <strong>and</strong> 1/(h s � h a) � 0.1272 lb/Btu (0.0609 kg/kJ).<br />

From Eq. (10.22), for each degree <strong>of</strong> increase in condenser water temperature, the corresponding<br />

increase in the enthalpy <strong>of</strong> <strong>air</strong> is<br />

Then at a condenser water temperature <strong>of</strong> 86°F, the enthalpy <strong>of</strong> saturated <strong>air</strong> film is 50.68 Btu/lb,<br />

<strong>and</strong> the enthalpy <strong>of</strong> the corresponding <strong>air</strong> in contact with this condenser water is<br />

h a � 41.59 � 1.2 � 42.79 Btu/lb<br />

The enthalpy difference between the saturated <strong>air</strong> film <strong>and</strong> <strong>air</strong> at T w � 86°F is then<br />

<strong>and</strong><br />

h s � h a � 50.68 � 42.79 � 7.89 Btu/lb<br />

1<br />

hs � ha dh a � m˙ w<br />

m˙ a<br />

� 1<br />

7.89<br />

REFRIGERATION SYSTEMS: COMPONENTS 10.45<br />

c pw dT w � (1.2 � 1) dT w<br />

� 0.1267 lb / Btu (0.0606 kg / kJ)<br />

TABLE 10.2 Numerical Integration <strong>of</strong> a Counterflow Cooling Tower for Example 10.2<br />

Cooling Enthalpy <strong>of</strong><br />

water saturated <strong>air</strong> Air enthalpy h s – h a,<br />

temperature, °F film h s, Btu/lb h a, Btu/lb Btu/lb<br />

1<br />

,<br />

hs � ha lb/Btu<br />

85 49.45 41.59<br />

Design conditions<br />

7.86 0.1272<br />

86 50.68 42.79 7.89 0.1267<br />

87 51.95 43.99 7.96 0.1256<br />

88 53.25 45.19 8.06 0.1241<br />

89 54.58 46.39 8.19 0.1221<br />

90 55.95 47.59 8.36 0.1196<br />

91 57.36 48.79 8.57 0.1167<br />

92 58.79 49.99 8.80 0.1136<br />

93 60.27 51.19 9.08 0.1101<br />

94 61.79 52.39 9.40 0.1064<br />

95 63.34 53.59 9.75 0.1026<br />

Part-load operation (50 percent design load)<br />

82 45.91 41.59 4.32 0.2315<br />

83 47.06 42.79 4.27 0.2341<br />

84 48.23 43.99 4.24 0.2358<br />

85 49.45 45.19 4.26 0.2347<br />

86 50.68 46.39 4.29 0.2331<br />

87 51.95 47.89 4.36 0.2294<br />

Average<br />

�Tw ,<br />

hs � ha �� ,<br />

lb/Btu�°F<br />

�Tw hs � h �<br />

a<br />

0.1270 0.1270<br />

0.1262 0.2532<br />

0.1249 0.3781<br />

0.1231 0.5012<br />

0.1209 0.6221<br />

0.1182 0.7403<br />

0.1151 0.8554<br />

0.1118 0.9672<br />

0.1082 1.0754<br />

0.1045 1.1799<br />

0.2328 0.2328<br />

0.2350 0.4678<br />

0.2402 0.7080<br />

0.2338 0.9418<br />

0.2312 1.1730

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