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Mass Transfer

Mass Transfer
Leaching rate is independent of the

None of the listed here
Temperature
Agitation
Particle size

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Mass Transfer
The change in enthalpy, when a unit quantity of gas is absorbed by relatively large quantity of adsorbent (on which a definite concentration of the adsorbed gas already exists) is termed as the

Differential heat of adsorption
Integral heat of adsorption
None of these
Heat of wetting

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Mass Transfer
Azeotropic distillation is employed to separate

Mixture with very high relative volatility
Heat sensitive materials
Constant boiling mixture
High boiling mixture

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Mass Transfer
Make up water is required in a cooling tower to replace the water lost by

Drift
All of these
Evaporation
Blowdown and leakage

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Mass Transfer
H₂S is being absorbed in a gas absorber unit. The height of the transfer unit based on the overall mass transfer coefficient on the gas side is 0.4 m. The equilibrium data is given by, y = 1.5 x. The bulk concentration of H₂S has to be reduced from 0.05 to 0.001 mole fraction in the gas side. The height of the tower (in metres) corresponding to an operating line given by, y = 5x + 0.001 is

0.56
1.56
1
2

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Mass Transfer
During constant rate period, the rate of drying decreases with the

Neither A nor B
Both A & B
Decrease in air temperature
Increase in air humidity

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