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Mass Transfer

Mass Transfer
Degree of freedom for leaching and solvent extraction process is

1
2
3

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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

0.175
0.25
0.4
0.2

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Mass Transfer
The most efficient cooling tower out of the following is

Forced draft
Induced draft
Natural draft
Atmospheric

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

Evaporation
Blowdown and leakage
Drift
All of these

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Mass Transfer
The surface renewal frequency in Danckwerts model of mass transfer is given by (KL: mass transfer co-efficient)

KL².DA
√(KL².DA)
KL²/DA
KL/DA²

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Mass Transfer
Absorption accompanied by heat evolution results in

Increase in equilibrium solubility
Decrease in equilibrium solubility
Increased capacity of the absorber
None of these

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