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Mass Transfer

Mass Transfer
Mass transfer co-efficient (K) and diffusivity (D) are related according to film theory as

K ∝ D
K ∝ D2
K ∝ D1.5
K ∝ √D

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

Minimum
Infinite
None of these
Optimum

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Mass Transfer
Sides of equilateral-triangular co-ordinates (on which ternary liquid system is plotted) represent

Partially miscible ternary system
A binary mixture
A ternary mixture
A pure component

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Mass Transfer
Unsaturated air (with dry bulb and wet bulb temperatures being 45°C and 25°C respectively) is passed through a water spray chamber maintained at 23°C. The air will be cooled and

None of these
Dehumidified
Humidified with wet bulb temperature decreasing
Humidified at constant wet bulb temperature

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Mass Transfer
Mass transfer co-efficient is defined as

Co-efficient = Flux/concentration difference
Flux = Co-efficient/concentration difference
None of the listed here
Flux=concentration difference/co-effi-cient

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Mass Transfer
CO₂ can be absorbed by

Alumina
Hot cupric oxide
Cold Ca(OH)₂
Heated charcoal

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