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Mass Transfer

Mass Transfer
Mechanism of moisture removal in case of freeze drying of food stuff is by

Sublimation
Adsorption
Dehydration
Evaporation

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Mass Transfer
The drying time between fixed moisture content within diffusion controlled 'falling rate period' is proportional to (assuming that drying occurs from all surfaces of the solid) (where, T = thickness of the solid )

T
√T
T³
T²

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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
0.2
0.4
0.25

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

Zero
Maximum
Minimum
Infinite

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Mass Transfer
The change in enthalpy, when a unit quantity of gas is absorbed by relatively large quantity of adsorbent (on which a definite concentration of the adsorbed gas already exists) is termed as the

Heat of wetting
Differential heat of adsorption
Integral heat of adsorption
None of these

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Mass Transfer
Back-trapping in a distillation column

Increases tray efficiency
Decreases tray efficiency
Is desirable, as it provides improved vapour-liquid contact
Reduces pressure drop

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