Cooling Tower Tank Design

It must also provide the energy head necessary to raise water from a low to a higher static head level.

Cooling tower tank design.

For the tower piping circuit the pump must overcome the piping flow friction loss. The majority of our cooling tower sump tanks are sandblasted interior to a near white followed by 7 to 11 mils dft of epoxy. Cooling towers may either use the evaporation of water to remove process heat and cool the working fluid to near the wet bulb air temperature or in the case of closed circuit dry cooling towers rely solely on air to cool the working fluid to near. Piping condenser cooling tower losses and valves.

If the tank has a flat bottom the exterior bottom of the tank should have a. Remote sump tanks can be added to cooling tower closed circuit cooling tower or evaporative condenser systems. Design and operation 2005 2018 trane a business of ingersoll rand. C approach to wet bulb temperature.

A trane engineers newsletter live cooling towers and condenser water systems. Cooling tower equipment louver motor pump tank. The required cooling tower design and size will be a function of following values. Cooling tower pump recirculation pump process pump stand by pump.

B web bulb temperature. All tanks have baffled compartments if required. If the tank has a flat bottom the exterior bottom of the tank should have a commercial blast followed by a coal tar epoxy to protect from the condensation. Cooling tower pumps are notorious for caviation and operating problems based on a bad sump design.

A cooling tower is a heat rejection device that rejects waste heat to the atmosphere through the cooling of a water stream to a lower temperature. Tank cover manufactured from stainless steel and supplied in sections for ease of removal and access covers are optional. Introduction a cooling tower is a heat rejection device which extracts waste heat to the atmosphere through the cooling of a water stream to a lower temperature. The majority of our cooling tower sump tanks are sandblasted interior to a near white followed by 7 to 11 mils dft of epoxy.

D mass flowrate of water circulation rate e air velocity through tower or individual tower cell. I suggest that you review the sump design suggestions conatined in the pump handbook karrassic et al and the information in the hydraulic institute standards cooling tower pumps require an additional npsh margin above the npsh required. If additional head pressure is a possibility the additional head pressure should be calculated and built into the design of the tank.