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Mass Transfer

Mass Transfer
Selectivity of the solvent used in solvent extraction should be

< 1
> 1
1

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Mass Transfer
Desulphurisation of petrol is done in a

Plate type extraction column
Rotating disc extractor
Bollman extractor
Packed extraction column

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

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Mass Transfer
The operating cost of a distillation column at minimum reflux ratio is

Maximum
Infinite
Minimum
Zero

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Mass Transfer
If moisture content of solid on dry basis is X, then the same on wet basis is

X/(X + 1)
(X + 1)/X
(X - 1)/X
X/(X - 1)

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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
10
6.89
8.89

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