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MASS TRANSFER

Mass Transfer
Absorption factor method is used to calculate the number of ideal stages, when

Operating line lies above the equilibrium line
Both operating and equilibrium lines are parallel
Operating line lies below the equilibrium line
Pressure drop in the column is very high

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Mass Transfer
Berl saddle made of carbon cannot be used for

SO₂
H₂SO₄
Alkalis
Oxidising atmosphere

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Mass Transfer
During constant rate period, the rate of drying decreases with the

Increase in air humidity
Neither A nor B
Decrease in air temperature
Both A & B

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Mass Transfer
At 750°K and 1 atm, the approximate value of Schmidt number for air is

0.01
1
10
0.1

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Mass Transfer
The reason for preferring packed towers over plate towers in distillation practice is that the packed tower operation gives

Low pressure drop and low hold up
Low pressure drop and high hold up
High pressure drop and low hold up
High pressure drop and high hold up

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