Mass Transfer
In a counter-current extractor, as the axial mixing increases, the extraction efficiency

Increases
Remains unchanged
Depends on the pressure of the system
Decreases

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Mass Transfer
In case of steam distillation, the steam leaving the liquid is not completely saturated with distillate vapour, because

Temperature is less
Saturated steam is used for steam distillation
Total pressure is less
Mixing of steam with the material being vaporised is not so intimate as to result in equilibrium condition

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Mass Transfer
In case of a desorber (stripper), the

Temperature remains unaffected
Operating line always lies above the equilibrium curve
Operating line always lies below the equilibrium curve
Temperature always increases

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