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3. If It is desired to strip 30 mol % of B from water into air. Outlet flowrate of air stream is 90kgmol/hr. Inlet composition

3. If It is desired to strip 30 mol % of B from water into air. Outlet flowrate of air stream is 90kgmol/hr. Inlet composition of B in air is 0.01mole%. Initially water with 18 mole % enters the multistage stripping process with a flow rate of 30kgmol/hr. BECAREFUL IT IS A STRIPPING PROCESS NOT AN ABSORPTION PROCESS! YB=2.5XB I a) Determine the # of theoretical stages by graphical approach b) Determine # of theoretical stages by Kremser equation c) If the tray efficiency is 50% what is the actual number of stages? Determine the maximum air stream flowrate and compare it with the value in the question. d) image text in transcribed
3. If It is desired to strip 30mol% of B from water into air. Outlet flowrate of air stream is 90kgmol/hr. Inlet composition of B in air is 0.01mole%. Initially water with 18 mole % enters the multistage stripping process with a flow rate of 30kgmol/hr. BECAREFUL IT IS A STRIPPING PROCESS NOT AN ABSORPTION PROCESS! YB=2.5B a) Determine the \# of theoretical stages by graphical approach b) Determine \# of theoretical stages by Kremser equation c) If the tray efficiency is 50% what is the actual number of stages? d) Determine the maximum air stream flowrate and compare it with the value in the

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