clear steps needed

Part C. Ammonia (NH3) in the gas stream is in contact with the pure liquid water stream, where the initial molar natio by volume was 3.85%. In this countereurrent packed bed tower, we want to reduce Ammonia concentration in the gas stream to 1%. The gas inlet flow rate per eross-sectional area is 52 mole/m m2s, and the ammonia-free water flow rate per eross-sectional area is 75moV m2s. The overall mole capacity coefficient, Kya, may be assumed to be 50mol/(msy). Answer the following questions. (10pt) Q1. Find inlet and outlet concentrations and draw an anakating line on the graph (7pt) Using the table below, find a height of the column ( 5pt ) Part C. Ammonia (NH3) in the gas stream is in contact with the pure liquid water stream, where the initial molar natio by volume was 3.85%. In this countereurrent packed bed tower, we want to reduce Ammonia concentration in the gas stream to 1%. The gas inlet flow rate per eross-sectional area is 52 mole/m m2s, and the ammonia-free water flow rate per eross-sectional area is 75moV m2s. The overall mole capacity coefficient, Kya, may be assumed to be 50mol/(msy). Answer the following questions. (10pt) Q1. Find inlet and outlet concentrations and draw an anakating line on the graph (7pt) Using the table below, find a height of the column ( 5pt )