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Table 1: SO₂-Water Equilibrium Data at 30 °C.
i. Determine the optimum liquid flow rate to be supplied in this packed tower by stating all relevant justifications.
ii. Determine the packed tower height, z if the major resistance to the mass transfer is in the gas phase.
Table 1: CH₃OH-water Equilibrium Data at 59.4 °C
i. Calculate the number of actual stages needed by using the analytical equation for overall tray efficiency of 25%, if the tower is desired to achieve at least 85% of CH₃OH recovery.
ii. Determine the optimum liquid flow rate by using 1.5 times the limiting rate and calculate the percentage of excess liquid solvent in this system.
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