Read: Chapter 22.1G-J The solute A is being absorbed from a gas mixture of A and B in a wetted-wall tower with the liquid flowing as a film downward along the wall. At the certain point in the tower the bulk gas concentration yAG=0.25 and the bulk liquid concentration xAL=0.13. The tower is operating at 298K and 1.013105Pa. The equilibrium data is shown below. The solute A diffuse through stagnant B in the gas phase and then through a non-diffusing liquid. By using correlations for diffusion solutions in wetted-wall towers, the film mass transfer for A in liquid phase as kx=1.8103kmol/m2s mol frac. 1. Calculate the interface concentration yAi and xAi and flux NA(60 points) 2. Calculate the overall mass transfer coefficient K'y and K'x. And flux NA (40 points) Read: Chapter 22.1G-J The solute A is being absorbed from a gas mixture of A and B in a wetted-wall tower with the liquid flowing as a film downward along the wall. At the certain point in the tower the bulk gas concentration yAG=0.25 and the bulk liquid concentration xAL=0.13. The tower is operating at 298K and 1.013105Pa. The equilibrium data is shown below. The solute A diffuse through stagnant B in the gas phase and then through a non-diffusing liquid. By using correlations for diffusion solutions in wetted-wall towers, the film mass transfer for A in liquid phase as kx=1.8103kmol/m2s mol frac. 1. Calculate the interface concentration yAi and xAi and flux NA(60 points) 2. Calculate the overall mass transfer coefficient K'y and K'x. And flux NA (40 points)