A heat exchanger with heat transfer surface area A and overall heat transfer coefficient U handles two fluids of heat capacities C1 and C2 such that C1 > C2. The NTU of the heat exchanger is given by 

1
AU/C1
2
AU/C2
3
\({e^{ - \left( {AU/{C_1}} \right)}}\)
4
\({e^{ - \left( {AU/{C_2}} \right)}}\)

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