Mass Transfer
The relative saturation of an unsaturated mixture of gas and vapor is independent of the

None of these
Temperature of the mixture
Composition of the mixture
Nature of the vapor

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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

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

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