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Handbook of air conditioning and refrigeration / Shan K

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50<br />

50<br />

Figure 27.9 shows the performance <strong>of</strong> an indirect-direct two-stage evaporating cooling VAV system<br />

if 1 percent dry-bulb <strong>and</strong> mean coincident wet-bulb (1 percent DB/MWB) temperatures, 1 percent<br />

wet-bulb <strong>and</strong> mean coincident dry-bulb (1 percent WB/MDB) temperatures, <strong>and</strong> 1 percent<br />

dew point <strong>and</strong> mean coincident dry-bulb (1 percent DP/MDB) temperatures <strong>of</strong> Denver, Colorado,<br />

are selected.<br />

From ASHRAE <strong>H<strong>and</strong>book</strong> 1997, Fundamentals, in Denver the outdoor design condition based<br />

on 1 percent wet-bulb temperature <strong>and</strong> the mean coincident dry-bulb temperature T o � has a dry-bulb<br />

temperature <strong>of</strong> 80°F (26.7°C) <strong>and</strong> 63°F (17.2°C). In an indirect evaporative cooler, if its effectiveness<br />

is 0.60, the temperature <strong>of</strong> cooled <strong>air</strong> discharged from the cooler is<br />

T� ca,l � 80 � 0.6(80 � 63) � 80 � 10.2 � 69.8�F(21.0�C)<br />

AC SYSTEMS: EVAPORATIVE COOLING 27.25<br />

Draw a line from point ca,l� that parallels the thermodynamic wet-bulb temperature line. With the<br />

saturation efficiency <strong>of</strong> the direct evaporating cooler � sat � 0.9, the cooled <strong>air</strong> leaves this direct<br />

evaporating cooler with a dry-bulb temperature <strong>of</strong> 60.3°F (15.7°C) <strong>and</strong> a relative humidity <strong>of</strong> 95<br />

percent.<br />

If the space temperature is maintained at 75°F (23.9°C) <strong>and</strong> if the sensible heat ratio <strong>of</strong> the<br />

space <strong>conditioning</strong> line is 0.9, the space relative humidity can be determined from the psychrometric<br />

chart to be 60 percent. The supply temperature differential used to calculate the supply volume<br />

flow rate is �T s � 75 � 60.3 � 14.7°F (8.2°C).<br />

Similarly, the performance <strong>of</strong> the indirect-direct two-stage evaporating cooling system using 1<br />

percent dry-bulb temperature <strong>and</strong> the mean coincident wet-bulb temperature, also 1 percent dew<br />

point temperature <strong>and</strong> the mean coincident dry-bulb temperature can be calculated as follows:<br />

s<br />

s�<br />

60<br />

s�<br />

ca,l�<br />

60<br />

T o �<br />

70<br />

ca,l<br />

ca,l�<br />

70<br />

r�<br />

r�<br />

r<br />

80<br />

80<br />

T o �<br />

90<br />

90<br />

T o<br />

100<br />

100<br />

To , �F<br />

w, lb/lb<br />

FIGURE 27.9 Comparison <strong>of</strong> 1 percent dry-bulb, 1 percent wet-bulb, <strong>and</strong> 1 percent dew point temperatures in Denver,<br />

Colorado.<br />

80%<br />

60%<br />

50%<br />

40%<br />

30%<br />

20%<br />

0.016<br />

0.012<br />

0.08<br />

0.04

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