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Mass Transfer

Mass Transfer
The slope of the operating line for a single component co-current absorber when plotted in terms of mole ratio units is

∞
+ve
-ve

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Mass Transfer
In a single stage extraction process, 10 kg of pure solvent S (containing no solute A) is mixed with 30 kg of feed F containing A at a mass fraction xf = 0.2. The mixture splits into an extract phase E and a raf-finate phase R containing A at xB = 0.5 and xR = 0.05 respectively. The total mass of the extract phase is (in Kg)

8.25
10
6.89
8.89

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

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

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Mass Transfer
Tower diameter may be decreased by

Increasing the liquid flow rate
Increasing the vapour flow rate
Using higher reflux ratio
Use of increased tray spacing

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Mass Transfer
With increase in temperature, the rate of extraction in leaching (solid-liquid extraction system)

Increases
Decreases
Increases Linearly
Remains unaffected

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Mass Transfer
The diffusivity (D) in a binary gas mixture is related to the temperature (T) as

D ∝ T0.5
D ∝ T2
D ∝ T1.5
D ∝ T

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