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INPUTS Flow Rate Temp IN Temp Out viscosity
OUTPUT 1800 45 33 0.72
GPM F F cp
Duty of cooling tower
5617.382 kW 1597.275 RT
Volume of basin
62.2 62.282 8244 44 m³
TDS content
Make Up Water Blowdown water Density Internal Dia For Circuit 1 efficiency of pump Volume of heat exchanger ID for side stream filter circuit Efficiency of pump
250 mg/lit 1200 mg/lit 1000 kg/m³ 10 in 80 % 1 m³ m³ 4 in 80 %
Circulation pump power
53.08954 kW 71.31523 bhp
Pressure Drop in lines of main circuit.
0.639463 psi/100ft
Fitter pump power
1.204651 kW 1.615862 bhp 0.790837 ps p si/100ft
Pressure drop in filter lines
ooling Tower Flow Rate
Q
Temp IN Temp Out Temp Diff
T1 T2 T1-T2
viscosity TDS content Make Up Water Blowdown water Cycle of Concentration Density
Pump Power Required Efficiency of pump 80 % Hydrulic Power
42471.633 42.471633 53.089541 57.052188 71.315235
Pump power Pump Power
Watt Kw Kw Hp bhp
Calculation Of Cooling Tower Duty Duty Of Cooling Tower
Q
5617.3824 kW 1597.27536 RT
Volume Circuit 1 Volume Of Suction Line V1 Volume Of Discharge Line V2 Volume of HEX V3 Volume of line to cooling tower V4 Total volume of circulating fluid V Circuit 2 Volume Of Suction Line V1 Volume of filter V2 Volume Of Discharge Line V3
4.572 m 15 ft Pressure Drop 44805.6 N/m² 6.5002943 Psi Pump Diffrential Pressure PD 84984.173 N/m² 12.32931 Psi Pump Power Required Efficiency of pump 80 % Hydraulic Power
Brake horse power
963.72052 watt 0.9637205 kW 1.2926896 hP 1.6158621 bHP 1.2046506 kW