13. The evaporative condenser of an ammonia refrigeration plant has a water flow rate of 100 kg/s and enters a natural draft cooling tower at 43oC. The water is cooled to 30oC by air entering at 27oC db 24oC wet bulb. The air leaves the tower as 90% RH and 32oC db. Calculate the percent of make-up water needed the tower. At 27oC db and 24oC wb: h = 72.5 KJ/kg, w = 0.0178 At 90% RH and 32oC db: h = 102 KJ/kg, w = 0.0275.
Water make-up (M ) = Total water losses = Drift Losses ( D) + Evaporation Losses (E ) + Blow down Losses (B)
D = 0.1 to 0.3 percent of Circulating water (C ) for an induced draft cooling tower
C = Circulating water in m3/hr
"\\lambda" = Latent heat of vaporization of water = 540 kcal/kg or 2260 kJ / kg
Ti – T0 = water temperature difference from tower top to tower bottom in °C ( cooling tower inlet hot water and outlet cold water temperature difference)
Cp = specific heat of water = 1 kcal/kg / °C (or) 4.184 kJ / kg / °C
C = 230 kg/s = (100 kg / 998 kg/m3) / (1/3600 h) = 360.72 m3/h
E = (830 m3/h x (40 - 30°C) x 4.184 kJ / kg / °C ) / 2260 kJ / kg = 15.4 m3/h
M = 360.72 x 0.1 + 15.4 = 51.47 m3/h
b) Cooling tower efficiency can be expressed as
μ = (ti - to) 100 / (ti - twb)
where
μ = cooling tower efficiency (%) - the common range is between 70 - 75%
ti = inlet temperature of water to the tower (oC)
to = outlet temperature of water from the tower (oC)
twb = wet bulb temperature of air (oC, oF)
μ = (40 - 30) / (40 - 26) * 100 = 71.4%
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