A packed counter-current water cooling tower is used to cool
1.356 kg/s.m2
of water from 43.3 °C to 26.7 ºC. The air enters from the bottom
of the tower at 23.9 ºC with a wet bulb temperature of 21.1 ºC. The whole of the
resistance to heat and mass transfer can be considered as being within the gas
phase and the product of the mass transfer coefficient and the transfer surface
per unit volume of column (KG.a) may be taken as 1.207×10-7
kmol/s.m3
.Pa.
The tower operates at atmospheric pressure. Calculate the minimum air flowrate
and the necessary height of the tower when 1.5 times of minimum is used as
actual air flowrate.
Data: Latent heat of water at 0 ºC = 2501 kJ/ kg
Heat capacity of dry air = 1.005 kJ/ kg. ºC
Heat capacity of water vapour = 1.88 kJ/ kg. ºC
Density of air = 1.198 kg/ m3
Enthalpy of saturated air-water vapour data are as follows:
Hyi, kJ/kg dry air 84 97.2 112.1 128.9 148.2 172.1 197.2
Temperature, ºC 26.7 29.4 32.2 35 37.8 40.6 43.3
The answer to your question is provided in the image:
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