When you know a heat exchanger’s size — captured by its overall conductance UA — but not the outlet temperatures, the ε-NTU method is the fastest way to find the heat duty. It expresses performance as a single dimensionless effectiveness that depends only on NTU, the ratio of the two streams’ heat-capacity rates, and the flow geometry. This calculator handles counter-flow, parallel-flow, and unmixed cross-flow units.
How it works
Each stream’s heat-capacity rate is its mass flow times specific heat, C = ṁ·cp. The smaller of the two is Cmin and the ratio Cr = Cmin/Cmax. The Number of Transfer Units is:
NTU = UA / Cmin
Cr = Cmin / Cmax
Effectiveness follows the arrangement. For counter-flow with Cr below 1:
eff = (1 - exp(-NTU(1 - Cr))) / (1 - Cr*exp(-NTU(1 - Cr)))
Parallel-flow uses (1 - exp(-NTU(1 + Cr))) / (1 + Cr), and unmixed cross-flow uses the Kays and London correlation. The actual duty and outlet temperatures then come from the maximum possible transfer:
q_max = Cmin * (T_hot_in - T_cold_in)
q = eff * q_max
T_hot_out = T_hot_in - q / C_hot
T_cold_out = T_cold_in + q / C_cold
Example and notes
Take a water-to-water counter-flow exchanger: hot stream 0.5 kg/s, cold 0.8 kg/s, both cp 4,186 J/kg·K, UA of 2,000 W/K, hot in 80°C, cold in 15°C. Cmin is the hot stream at 2,093 W/K, Cr is 0.625, NTU is about 0.956, and effectiveness lands near 0.55. The hot stream leaves around 44°C and the cold stream rises to roughly 36°C.
Effectiveness never exceeds 1, and for a fixed UA the only way to raise it is to lower the flow rates (raising NTU) or switch to a counter-flow layout. Use this to size HRV cores, hydronic plate exchangers, and water-to-water loops; for multi-pass shell-and-tube units apply the appropriate correction factor instead.