Mass Transfer
Use of packed towers for distillation is generally limited to the

High pressure operation
Small sizes
Vacuum distillation
Multicomponent distillation

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

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
Pr = Sc ; there won
Both A & B

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