A counter-current absorption column operates at 400K and 850kPa. The absorbent liquid is high molecular mass oil which contains 0.275% of the heaviest component, C7H16, but none of the lighter components. The total molar flowrate of the oil entering the absorber is 185kmol/hr. The effluent gas enters the absorber at 850kmol/hr and its composition is given in Table 1. Table 1. Composition of effluent gas and Kivalues for components There are 5 stages in the column (N=5) to remove as much of the heaviest component (C7H16) from the effluent gas as possible. 1 SPP3701 Assessment 042023 S1 2.1. Calculate the molar flowrates of the components entering the absorber in the liquid stream and the effluent gas stream. Tabulate your answers. (4) 2.2. Calculate the compositions and flowrates of the vapor (V) and liquid (L) streams leaving the absorber. Tabulate your answers in an appropriate format. A counter-current absorption column operates at 400K and 850kPa. The absorbent liquid is high molecular mass oil which contains 0.275% of the heaviest component, C7H16, but none of the lighter components. The total molar flowrate of the oil entering the absorber is 185kmol/hr. The effluent gas enters the absorber at 850kmol/hr and its composition is given in Table 1. Table 1. Composition of effluent gas and Kivalues for components There are 5 stages in the column (N=5) to remove as much of the heaviest component (C7H16) from the effluent gas as possible. 1 SPP3701 Assessment 042023 S1 2.1. Calculate the molar flowrates of the components entering the absorber in the liquid stream and the effluent gas stream. Tabulate your answers. (4) 2.2. Calculate the compositions and flowrates of the vapor (V) and liquid (L) streams leaving the absorber. Tabulate your answers in an appropriate format