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Mass Transfer

Mass Transfer
According to Chilton-Colburn analogy for mass transfer, NSt.NSc2/3 is equal to

2f
F/2
1/f
F

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Mass Transfer
In gas-liquid contact operation, the number of ideal stages, N = (xa - xb)/(xb - x*b) . This is true when the stripping factor 'S' is

S = 1
S = ∞
S < 1
S > 1

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Mass Transfer
The binary diffusivity in gases does not depend upon the

Temperature
None of the listed here
Nature of the components
Pressure

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Mass Transfer
For a distillation column operating at minimum reflux, the

None of these
Concentration of liquid and vapour leaving a plate will be same
Reflux ratio will be maximum
Number of plates required will be maximum

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Mass Transfer
The Hatta number is important in

Binary distillation
Multicomponent distillation
Gas absorption with chemical reaction
Gas absorption without chemical reaction

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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)

8.25
8.89
6.89
10

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