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Mass Transfer

Mass Transfer
Rate of leaching increases with increasing

Viscosity of solvent
Pressure
Temperature
Size of the solid

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Mass Transfer
Unit operation involved in the prilling of urea is

Crystallisation
Both B and C
Evaporation
Drying

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Mass Transfer
The interfacial area per unit volume of dispersion, in a gas-liquid contactor, for fractional hold up of gas = 0.1 and gas bubble diameter = 0.5 mm is given by (in m²/m³)

50
100
500
1000

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Mass Transfer
Air initially at 101. 3 kPa and 40°C and with a relative humidity of 50%, is cooled at constant pressure to 30°C. The cooled air has a

Higher dew point
Higher relative humidity
Higher absolute (specific) humidity
Higher wet bulb temperature

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Mass Transfer
Boiling point diagram is

Not affected by pressure
A plot of temperature vs. vapour composition
Affected by pressure
A plot of temperature vs. liquid composition

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Mass Transfer
Absorption accompanied by heat evolution results in

Increase in equilibrium solubility
Decrease in equilibrium solubility
None of these
Increased capacity of the absorber

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MORE MCQ ON Mass Transfer

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