For the system shown in the figure and based on the degree-ot-freedom analysis, a system with which the material balance might appropriately begin is: no (kg H,0) Mixing point Evaporator Splitting point m m. 1 012 kg S 012 kg S/kg 088 ke 10/kg 088 kg 1.0/ kg/ kg HO/kg 0.42 kg: S/ky 0.58 kg HOR m 1 012 SL 038 kg H0/kg