In an absorption process for recovering NH, from a gas stream composed of Nz and NHs. Flowing upward through the process is the gas stream, which contain NH, and Nz but not solvent S, and flowing downward through the device is a liquid stream which contain NH, and liquid S but not N2. The mol fraction of NH3 in the leaving gas stream is half of the mol fraction of NH, in the leaving liquid stream from absorber. Calculate flow rates and composition of gas and liquid streams leaving the absorber column. (Given that gas stream entering the absorber with flow rate of 1000 Kg/hr contains 10 mol% NH3 and 90 mol% N2, and liquid stream entering the absorber with flow rate of 1000 Kg/hr contains pure solvent S). [1.5+1.5+51