A liquid stripping process is used to transfer hydrogen sulfide (H2S) dissolved in water into a contacting air stream. The solvent (water) and carrier gas (air) are assumed to be immiscible, and the solvent is not volatile. At the present conditions of operation, the composition of H2S in the bulk gas phase is 1 mole %, and in the liquid phase is 0.006 mol% or 112 mg H2S/L. The individual mass transfer coefficients are k = 0.30 kgmole/ms for the liquid film, and k = 4.5x10^-5 kgmol/m.s for the gas film. The temperature is 20°C and the total system pressure is 1.5 atm. The density of the liquid approaches the density of liquid water at 20°C, which is 992.3 kg/m^3. The equilibrium line for the HS-water-air system at 20°C is provided below. Plot the operating point. Determine m, the equilibrium distribution coefficient. Estimate the overall mass-transfer coefficients Kg and K. Determine the flux from the liquid phase to the gas phase and the interface compositions PA.i and cALi.