Cooling Tower Range, Approach and Condenser Water Flow Calculator

Work out a tower’s range, approach and heat rejection from its water temperatures and flow — or the condenser water flow a chiller needs.

Method reviewed October 26, 2026. Version 1.0.0. How it works

Your inputs

Unit system

Result

Range (entering − leaving water)
10°F
Approach (leaving water − wet bulb)
7°F
Heat rejected
1,500,000BTU/h

Range 10 °F, approach 7 °F, rejecting 1,500,000 BTU/h.

  • A tower’s rated (nominal) tons are its capacity at one rating condition: 3 gpm per ton cooled from 95 °F to 85 °F at a 78 °F wet bulb, which is 15,000 BTU/h. At other conditions the same tower rejects a different amount; use the manufacturer’s selection data.
Heat rejected ÷ 15,000 BTU/h (nominal tower-ton basis)
100nominal tower tons
Range ÷ (range + approach)
59%
Show the working
  1. Range = entering − leaving water
    95 − 85 = 10 °F
  2. Approach = leaving water − entering wet bulb
    85 − 78 = 7 °F
  3. Heat rejected = 500 × gpm × range
    500 × 300 × 10 = 1,500,000 BTU/h

Range and approach

The range is the temperature drop of the water through the tower: entering hot water minus leaving cold water. The approach is how close the leaving water gets to the entering air’s wet-bulb temperature. A tower can never cool water to the wet bulb, so the approach is always above zero.

Heat rejected by the water = 500 × gpm × range.

Condenser water flow for a chiller

The condenser water carries away the chiller’s cooling load plus its compressor energy: heat rejected = capacity × (1 + 1/COP). At a COP of 4, a 100-ton chiller rejects 1.5 million BTU/h, which at a 10 °F range is 300 gpm — 3 gpm per ton.

That is the origin of the nominal “tower ton”: cooling 3 gpm from 95 °F to 85 °F at a 78 °F wet bulb, or 15,000 BTU/h. A tower’s capacity at other conditions comes from the manufacturer’s selection data.

Worked example

These are the example values the calculator opens with, and the result the engine calculates for them.

Inputs

Calculate
Tower range, approach and heat rejection
Hot water entering the tower
95 °F
Cold water leaving the tower
85 °F
Entering air wet-bulb temperature
78 °F
Water flow through the tower
300 gpm

Result

Range (entering − leaving water)
10 °F
Approach (leaving water − wet bulb)
7 °F
Heat rejected
1,500,000 BTU/h
Heat rejected ÷ 15,000 BTU/h (nominal tower-ton basis)
100 nominal tower tons
Range ÷ (range + approach)
59 %

Range 10 °F, approach 7 °F, rejecting 1,500,000 BTU/h.

Assumptions

  • Heat rejected by the water = 500 × gpm × range (water at about 8.33 lb/gal).
  • Chiller heat rejection = capacity + compressor input = capacity × (1 + 1/COP).

Limitations

  • Evaporation, drift and blowdown are not calculated.
  • Tower capacity at other conditions comes from the manufacturer’s selection data; this tool does not predict the approach a tower can reach.

Frequently asked questions

Why is a cooling tower ton 15,000 BTU/h?

It includes the compressor heat: 12,000 BTU/h of cooling plus about 3,000 BTU/h of compressor energy for a chiller with a COP of about 4.

What approach can a tower reach?

It depends on the tower size and design and the conditions; the manufacturer’s selection data shows what a given tower can do.

Does this calculate evaporation or blowdown?

No. Those depend on the water treatment and cycles of concentration, which this tool does not cover.

Sources

  1. Notes for products (nominal capacity definitions) — Baltimore Aircoil Company. Nominal tons of cooling: the capability to cool 3 USGPM of water from 95 °F entering to 85 °F leaving at a 78 °F entering wet-bulb temperature.
  2. Best Practices Guide for Energy-Efficient Data Center Design (revised July 2024) — U.S. Department of Energy, Federal Energy Management Program. For a given cooling load, larger cooling towers have a smaller approach to the ambient wet-bulb temperature, allowing lower condenser water temperatures and better chiller efficiency (p. 26).
  3. University Physics Volume 2, §4.3 Refrigerators and Heat Pumps — OpenStax, Rice University (CC BY 4.0). Energy conservation W = Q_h − Q_c; refrigerator coefficient of performance K_R = Q_c ÷ W; heat pump K_P = Q_h ÷ W.
  4. NIST Guide to the SI (SP 811), Appendix B.9 — conversion factors — National Institute of Standards and Technology. 1 ton of refrigeration = 12,000 BTU/h; 1 BTU/h = 0.2930711 W; 1 atm = 101.325 kPa.

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