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Mass Transfer

Mass Transfer
In a binary distillation column, if the feed contains 40 mole % vapour, the q line will have a slope of

0.6
-0.6
1.5
-1.5

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Mass Transfer
Diffusivity in concentrated solutions differs from that in dilute solutions, because of the changes in

Neither A nor B
Degree of ideality of the solution
Both A & B
Viscosity with concentration

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Mass Transfer
In case of physical adsorption, the difference between heat of adsorption and heat of normal condensation is

Called integral heat of adsorption
Zero
Equal to the heat of formation of surface compound
Equal to the heat of wetting

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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)

8.89
8.25
10
6.89

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Mass Transfer
Flash distillation is suitable for the separation of components

Having very wide boiling points
Having very close boiling points
Which form maximum boiling azeotrope
Which form minimum boiling azeotrope

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Mass Transfer
Diffusion co-efficient generally depends upon the temperature, pressure & the nature of the components of the system. Its dimension is not the same as that of the

Volumetric diffusivity
Kinematic viscosity
Mass transfer co-efficient
Thermal diffusivity

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