Mass Transfer
Priming in a distillation column

Reduces the overall pressure drop
Is characterised by the presence of foam throughout the space between trays
Is desirable from point efficiency consideration
Results from very low gas velocity

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

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

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