Mass Transfer
In case of absorption with exothermic reaction, for fluids having

Both A & B
Pr = Sc ; there won
Pr = Sc; percentage change in heat and mass transfer flux will be the same for a given change in the degree of turbulence
Pr = Sc = 1; total mass, momentum and thermal diffusivity will be the same

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Mass Transfer
To get high tray efficiency

Liquid entrainment should be severe
Gas velocity should be very low
Time of contact between the two phases should be less
Interfacial surface between liquid and gas phase should be large

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