Mass Transfer
The dew point of an unsaturated gas-vapor mixture does not depend upon the __________ of the mixture.

All of these
Composition
Total pressure
Temperature

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Mass Transfer
Experiments were conducted to determine the flux of a species A in a stagnant medium across a gas-liquid interface. The overall mass transfer co-efficient based on the liquid side for dilute systems for the above was estimated to be 4 x 10⁻³ kg mole/m².s. The equilibrium data for the system is given as y = 2x. The flux across the interface (in kg mole/m² .s) for bulk concentrations of A in gas phase and liquid phase as y = 0.4 and x = 0.01 respectively is

8.5 x 10⁻³
5.6 x 10⁻⁴
5.6 x 10⁻³
8.5 x 10⁻⁴

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Mass Transfer
To get high tray efficiency

Liquid entrainment should be severe
Interfacial surface between liquid and gas phase should be large
Gas velocity should be very low
Time of contact between the two phases should be less

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