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Mass Transfer

Mass Transfer
Surface renewal model of mass transfer was enunciated by

Fick
Danckwerts
Stefan
Toor and Marchello

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Mass Transfer
At what value of reflux ratio, number of theoretical plates in a distillation column is minimum?

1
∞
< 1

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Mass Transfer
In stripping section of continuous distillation column, the

None of these
Liquid is enriched with high boiler
Liquid is stripped of high boiler
Vapour is stripped of low boiler

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Mass Transfer
The reason for preferring packed towers over plate towers in distillation practice is that the packed tower operation gives

High pressure drop and low hold up
Low pressure drop and low hold up
High pressure drop and high hold up
Low pressure drop and high hold up

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Mass Transfer
The change in enthalpy per unit weight of adsorbed gas when adsorbed on gas free or "outgassed" adsorbent to from a definite concentration of adsorbate is called its

Heat of wetting
Integral heat of adsorption
Differential heat of adsorption
Heat of normal condensation

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Mass Transfer
1 kg of a saturated aqueous solution of a highly soluble component A at 60°C is cooled to 25°C. The solubility limits of A are (0.6 kgA/kg water) at 60°C and (0.2 kgA/kg water) at 25°C. The amount in kg of the crystals formed is

0.4
0.2
0.175
0.25

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