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Cooling Tower Efficiency

Reference data and engineering information about cooling tower efficiency for hvac systems applications.

coolingtowerefficiencyCalculator

Overview

Engineering reference data for Cooling Tower Efficiency in HVAC systems.

Key Formulas

Sensible Heat

Q=m˙cpΔTQ = \dot{m} c_p \Delta T

Heat causing temperature change.

Latent Heat

Q=m˙hfgΔωQ = \dot{m} h_{fg} \Delta\omega

Heat causing moisture change.

COP (Cooling)

COP=Qc/WCOP = Q_c / W

Coefficient of performance.

Variables

SymbolDescriptionUnit
QQHeat transferW
m˙\dot{m}Mass flow ratekg/s
cpc_pSpecific heat of airJ/(kg·K)
ΔT\Delta TTemperature differenceK

Types of Cooling Towers

Cooling towers are primarily categorized into two types: forced draught and natural draught. Both rely on evaporative cooling. Forced draught towers utilize fans to circulate air, while natural draught towers depend on temperature gradients and wind forces. Natural draught towers exhibit more variable efficiency over time and are generally less efficient than forced draught systems.

Water Consumption and Make-Up Water

The make-up water requirement for a cooling tower is approximately 0.2–0.3 liters per minute per ton of refrigeration. This represents a significant reduction in water usage compared to traditional city water systems, with potential savings of 90–95%.

Temperature Ranges and Efficiency Limits

The temperature difference between inlet and outlet water, known as the range, is typically 10–15°F (approximately 5.5–8.3°C). The approach is the difference between the cooled water outlet temperature and the entering air wet bulb temperature. For evaporative cooling, the maximum achievable efficiency is inherently limited by the wet bulb temperature of the ambient air.

Safety and Maintenance Note

Cooling towers, due to their medium-temperature operation, can harbor pathogenic bacteria such as those causing Legionnaires' disease. Rigorous cleaning and regular maintenance are essential to mitigate this risk and ensure system safety.

References