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
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