Problem 3 G1-1.665 kmol/h of a binary gas mixture containing ammonia (vi-35%, molar basis) and air enter an absorpt...
Problem 3 G1-1.665 kmol/h of a binary gas mixture containing ammonia (vi-35%, molar basis) and air enter an absorption column operating at 1 atm and 20 °C, where a liquid mixture of water and ammonia (x-2.11%, molar basis) is used to remove 90% of the ammonia from the gas stream. Equilibrium data for this system is given in the table below: (kg NH;) / (100 kg Partial pressure of NH H2O) Mole fraction of NHs in Mole fraction of NHs in liquid,x 0.02073 in gas phase, mmHg 12.0 gas, y 0.01578 0.04171 0.05027 31.7 0.09574 0.1371 0.09158 10 69.6 114 0.1500 15 0.2184 0.1748 166 20 0.2096 0.2411 0.2987 0.3921 227 298 25 30 For (Ls/Gc) -2.38, determine graphically the number of equilibrium stages required for this separation. Try to determine N from the Kremser equation (you would need first to fit the equilibrium line to a straight line, y -mx), and compare both results.
Problem 3 G1-1.665 kmol/h of a binary gas mixture containing ammonia (vi-35%, molar basis) and air enter an absorption column operating at 1 atm and 20 °C, where a liquid mixture of water and ammonia (x-2.11%, molar basis) is used to remove 90% of the ammonia from the gas stream. Equilibrium data for this system is given in the table below: (kg NH;) / (100 kg Partial pressure of NH H2O) Mole fraction of NHs in Mole fraction of NHs in liquid,x 0.02073 in gas phase, mmHg 12.0 gas, y 0.01578 0.04171 0.05027 31.7 0.09574 0.1371 0.09158 10 69.6 114 0.1500 15 0.2184 0.1748 166 20 0.2096 0.2411 0.2987 0.3921 227 298 25 30 For (Ls/Gc) -2.38, determine graphically the number of equilibrium stages required for this separation. Try to determine N from the Kremser equation (you would need first to fit the equilibrium line to a straight line, y -mx), and compare both results.