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Mass Transfer

Mass Transfer
If f = moles of vapour present per mole of feed, then the slope of feed line is

- (f - 1)/f
(1 - f)/f
- 1/f
- f/(1 - f)

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Mass Transfer
The value of Lewis number (Le = Sc/Pr) for air-water vapour system is around

3.97
1
600
0.24

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Mass Transfer
In case of gases, the binary diffusivity is proportional to (where, P = pressure)

1/√P
√P
P
1/P

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Mass Transfer
In a single stage extraction process, 10 kg of pure solvent S (containing no solute A) is mixed with 30 kg of feed F containing A at a mass fraction xf = 0.2. The mixture splits into an extract phase E and a raf-finate phase R containing A at xB = 0.5 and xR = 0.05 respectively. The total mass of the extract phase is (in Kg)

10
6.89
8.25
8.89

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Mass Transfer
For a fixed number of ideal stages in a distillation column, as the reflux ratio is increased, the difference in composition between the top and bottom product streams

Increases
Passes through a maximum
Decreases
Remains unaffected

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Mass Transfer
The caking of crystals can be prevented by

Coating the product with inert material
Maintaining low critical humidity
Both A and C
Maintaining high critical humidity

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