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Mass Transfer

Mass Transfer
Desirable value of absorption factor in an absorber is

0.5
> 1
1
< 1

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Mass Transfer
Drift in a cooling tower is

Dependent on the water lost by evaporation
All of these
The water entrained by the circulating air
Desirable

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Mass Transfer
As the reflux ratio increases, the slope of the operating line for rectifying section

Decreases
Increases
Data insufficient, cannot be predicted
Remains constant

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Mass Transfer
Equilibrium-moisture curves of different solids

None of these
Are different
Are same
Depend on the humidity of the gas

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Mass Transfer
Fenske equation determines the

Maximum number of ideal plates
Optimum reflux ratio
Height of the distillation column
Minimum number of theoretical plates

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Mass Transfer
According to Chilton-Colburn analogy for mass transfer, NSt.NSc2/3 is equal to

2f
F
1/f
F/2

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