xA/0, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35

yA/0, 0.022, 0.052, 0.087, 0.131, 0.187, 0.265, 0.38

- A solute component is being diffused from a gas mixture of in a wetted wall column in figure below. At a certain point in the column the gas bulk contains 0.391 mole fractions of the solute and its concentration at the liquid bulk was 0.12 mole fraction. If the solute is diffusing through stagnant layer of the second component and then through non, diffusing liquid. Given the individual mass transfer coefficient for equi molar mass transfer for both gas and liquid phases 1.46 * 10 - Kg mole solute /s.m? mole fraction and 1.93 * 10 - (Kg mole solute/ s.m mole fraction), respectively. I. Calculate the flux and overall mass transfer coefficient based on gas phase. II. What will be the percent resistance in the gas and liquid films of the total resistance. Gas Liquid Liquid Gas