In the following we show a schematic diagram
of a cooling tower in the context of a steam power plant:
Referring to the diagram above the mass flow rate of the makeup water is given by the difference in specific humidity ω at the inlet and outlet air streams multiplied by the mass flow rate of the dry air. Thus the mass flow balance equations for the cooling tower become:
Since no work is done and no heat transfered externally, the cooling tower energy equation reduces to an enthalpy balance equation. Combining the mass flow equations with the energy equation leads to the final equation relating the mass flow rate of the dry air to the circulating cooling water of the condenser, as follows:
The mass flow rate of the liquid water at stations (3) and (4) is normally provided from the condenser energy equation of the steam power plant. Recall from Chapter 10a that the specific humidity ω is related to the various pressures and the relative humidity φ by the following relations:
The pressure Pv is the partial pressure of the vapor, Pg is the saturation pressure at temperature T, and P is the total pressure (air + vapor), usually taken as one atmosphere (101.325 kPa). In Chapter 10b we saw how all of these relations can be most conveniently evaluated graphically on a Psychrometric Chart. Notice that we have extended the moisture specific humidity range on this chart from 30 to 40 grams/kg-air in order to accomodate the extremely high humidity normally encountered at at station (2), which is the reason why we normally see a cloud above the cooling tower.
Note that the enthalpies of the vapor (h1 and h2) and those of the liquid (h3, h4, hmu) can be conveniently evaluated as follows:
The temperature T is in degrees Celsius, and the specific heat capacity of dry air CP is approximately 1.00 [kJ/kg°C] and that of liquid water approximately 4.18 [kJ/kg°C]. In the above analysis we have assumed that the temperature of the makeup water Tmu equals the temperature of the cooled circulating water T3. Alternatively the values of enthalpy for the vapor (h1 and h2) can also be conveniently read directly from the Psychrometric Chart.
Solved Problem 10.5 - Cooling Tower for the Supercritical Steam Power Plant for Athens, Ohio
Problem 10.6 - Cooling Tower for the Cogeneration Steam Power Plant for Ohio University
Engineering Thermodynamics by Israel Urieli is licensed under a Creative Commons Attribution-Noncommercial-Share Alike 3.0 United States License