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NCT 171

Effect of Low Approach vs High Approach in Cooling Tower

Approach is one of the most critical performance indicators for a cooling tower. It’s defined as:

text

Approach = Cold Water Temperature (CWT) – Wet Bulb Temperature (WBT)

Where:

  • Cold Water Temp = Temperature of water leaving the tower basin
  • Wet Bulb Temp = Lowest possible temperature theoretically achievable

This simple difference has profound implications for design, operation, and economics.

LOW APPROACH (Typically 5-10°F / 3-6°C)

What It Means

The tower is cooling the water very close to the wet bulb limit. Example: WBT = 78°F, CWT = 83°F → Approach = 5°F.Advantages

  1. Better Process Cooling:
    • Lower cold water temperature improves heat exchanger efficiency
    • Increases production capacity in industrial processes
    • Lowers condenser pressure in chillers, reducing compressor energy
  2. Energy Savings Downstream:
    • Chillers require less work to produce chilled water
    • Refrigeration systems operate more efficiently

Disadvantages & Costs

  1. Larger Tower Size:
    • Requires significantly more heat transfer surface (fill area)
    • Larger fans, motors, and structure
    • Capital cost increases exponentially as approach decreases
Approach ReductionTower Cost Increase
10°F to 8°F~15-20% larger
8°F to 6°F~25-35% larger
6°F to 4°F~40-60% larger
  1. Higher Operating Costs:
    • Increased fan energy consumption (more airflow required)
    • Higher pumping head may be needed
    • More sensitive to fouling and poor maintenance
  2. Operational Sensitivity:
    • More vulnerable to performance degradation
    • Small changes in WBT or airflow have bigger impacts
    • Requires excellent water treatment and maintenance

HIGH APPROACH (Typically 10-20°F / 6-11°C or higher)

What It Means

The tower is operating far from its theoretical limit. Example: WBT = 78°F, CWT = 95°F → Approach = 17°F.

Advantages

  1. Smaller, Cheaper Tower:
    • Less fill surface area required
    • Smaller fans and motors
    • Significantly lower capital cost
  2. Forgiving Operation:
    • Less sensitive to minor fouling
    • Can tolerate some maldistribution
    • More stable performance with varying loads
  3. Lower Fan Energy:
    • Reduced airflow requirements
    • Smaller motors with lower operating costs

Disadvantages & Problems

  1. Poor Process Performance:
    • Higher cold water temperature reduces heat exchanger effectiveness
    • May limit production capacity
    • Increases energy consumption in downstream equipment
  2. Usually Indicates Problems:
  1. For an existing tower, a high approach is a RED FLAG
  2. Typically caused by:
    • Fouled fill (scale, algae, sediment)
    • Low airflow (fan problems, clogged inlets)
    • Water maldistribution (clogged nozzles)
    • Overloading (exceeding design capacity)
  3. Higher Overall System Energy:
    • While tower fan energy is lower, the total system energy is often higher
    • Compressors, chillers, and pumps work harder due to warmer water