If one of the two fluids flowing through a heat exchanger of NTU = 2 remains at constant temperature throughout the exchanger length, the effectiveness of the heat exchanger will be

1
1 – e-4
2
1 – e-2
3
\(\dfrac{{1 - {e^{ - 2}}}}{2}\)
4
\(\dfrac{{1 - {e^2}}}{2}\)

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