Heat Exchanger Efficiency Explained: Effectiveness, U-Value and Approach
Heat exchanger efficiency is measured by effectiveness, the overall heat transfer coefficient (U-value) and approach temperature. Here is what each means.
What 'efficiency' means for a heat exchanger
There is no single efficiency number for a heat exchanger. Three related measures describe performance: effectiveness (how close it gets to the maximum possible heat transfer), the overall heat transfer coefficient or U-value (how readily heat crosses the surface), and the approach temperature (the smallest temperature gap between the two streams). A good design balances all three against pressure drop and cost.
Effectiveness and the NTU method
Effectiveness is the actual heat transferred divided by the maximum thermodynamically possible for the given inlet temperatures and flow rates. Engineers calculate it with the effectiveness-NTU (number of transfer units) method. Plate heat exchangers routinely reach 90%+ effectiveness in counter-flow because their corrugated channels create near-true counter-current flow; shell-and-tube units are typically lower unless multiple passes are used.
Overall heat transfer coefficient (U-value)
The U-value (W/m²·K) combines the film coefficients of both fluids, the wall conductance and any fouling resistance. Higher U means more heat transferred per unit area, so a smaller, cheaper unit. Plate exchangers achieve U-values three to five times those of shell-and-tube units because turbulent, thin-film flow over corrugated plates gives very high film coefficients.
Approach temperature
Approach is the difference between the outlet of one stream and the inlet of the other. A close approach (1–2 °C) means more heat recovered but requires more surface area. Plate units can economically achieve a 1 °C approach; shell-and-tube units rarely go below 5 °C. Close approaches matter most in heat-recovery and free-cooling duties where every recovered degree saves energy.
What reduces efficiency in service
Fouling adds thermal resistance and cuts the U-value; flow below design lowers turbulence and the film coefficient; air or non-condensables blanket the surface in condensing duties; and bypass from failed gaskets reduces effective area. Monitoring approach temperature and pressure drop catches efficiency loss early.
Getting an efficient selection from Jiangxing
Shanghai Jiangxing's engineering team sizes plate and shell-and-tube units to your target effectiveness and approach, balancing surface area, pressure drop and cost. Send your duty, temperatures and flow rates to Evan, jxmike@shheatex.com, or WhatsApp +86 173 1725 8304 for an efficiency-optimised selection.
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