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NCT 173

Practical Implications of the Relationship

The Fixed Relationship: If You Know Two, You Know the Third

Given the equation H = Q × R × C, these relationships are mathematically locked:

If This Changes…And This Is Held Constant…Then This Must…
Heat Load (H) ↑Flow Rate (Q)Range (R) ↑
Heat Load (H) ↑Range (R)Flow Rate (Q) ↑
Flow Rate (Q) ↑Heat Load (H)Range (R) ↓
Flow Rate (Q) ↑Range (R)Heat Load (H) ↑
Range (R) ↑Heat Load (H)Flow Rate (Q) ↓
Range (R) ↑Flow Rate (Q)Heat Load (H) ↑

Real-World Example:

A cooling tower designed for: H = 1,000 TR (12,000,000 BTU/h

If the actual flow drops to 2,400 GPM but the heat load remains 1,000 TR, then:

  • New Range = 12,000,000 ÷ (2,400 × 500) = 10°F
  • The tower must provide a 10°F range instead of 8°F, which it may not be able to do!

4. Design Perspective

The Design Triangle

Engineers typically fix two parameters and calculate the third:

Common Design Scenarios:

  1. Known Process: “My process rejects X BTU/hr, and I have Y GPM available”
    → Calculate required Range: R = H ÷ (Q × 500)
  2. Known Temperature Requirements: “I need to cool from 95°F to 85°F (R=10°F) with Z BTU/hr”
    → Calculate required Flow: Q = H ÷ (R × 500)
  3. Existing Tower Evaluation: “I have a 1,500 GPM tower with 10°F range”
    → Calculate capacity: H = 1,500 × 10 × 500 = 7,500,000 BTU/hr (625 TR)

Typical Design Values by Application:

ApplicationTypical RangeTypical Flow/TRNotes
HVAC Chiller Condenser8-12°F2.5-3.0 GPM/TR24 ÷ Range = GPM/TR
Power Plant Condenser20-30°F1.5-2.0 GPM/TRLarge ΔT, lower flow
Process Cooling10-25°FVaries widelyDepends on process
Plastics Cooling5-15°F2.0-4.0 GPM/TRSensitive temperature control