Heat Transfer
The advantage of using a 1 - 2 shell and tube heat exchanger over a 1 - 1 shell and tube heat exchanger is

Lower tube side pressure drop
Higher shell side heat transfer co-efficient
Lower shell side pressure drop
Higher tube side heat transfer co-efficient

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Heat Transfer
If Prandtl number is greater than the Schmidt number, then the

thermal boundary layer lies inside the concentration boundary layer
none of the listed here
thermal & concentration boundary layers are of equal thickness
concentration boundary layer lies inside the thermal boundary layer

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