Mass Transfer
As complete saturation of an adsorbent is approached, the differential heat of adsrop-tion approaches

That of normal condensation
Integral heat of adsorption
None of these
Zero

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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 ; there won
Both A & B
Pr = Sc = 1; total mass, momentum and thermal diffusivity will be the same

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