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Suethanol saturated solution, of which 58% by weight is ethanol (C2H5OH) and 45% condensed as a result of heating and cooling, is fed to the

Suethanol saturated solution, of which 58% by weight is ethanol (C2H5OH) and 45% condensed as a result of heating and cooling, is fed to the distillation column at a molar rate of 250 kmol/h. The bottom product composition is 5% mole of ethanol, while 20% by mole of the stream exiting the full concentrator integrated with the column is water. It is given that the backflow rate used throughout the process is RD=1.4RD,min. Ptotal= 1 atm. and T= 298 K, the liquid-vapor equilibrium curve data of the ethanol-water mixture are given. Accordingly, answer the following questions. x /0 0.02 0.07 0.12 0.24 0.3 3 0.4 y /0 0.18 0.39 0.47 0.55 0.58 0.51 0.52 0.57 0.68 0.75 0.89 0.61 0.66 0.66 0.68 0.74 0.78 0.90 a) Write down the slope of the supply line and the equation of the q line b) Calculate the top and bottom product flow rates. c) Calculate the vapor and liquid flow rates in the enrichment and stripping zones. d) Calculate the minimum backflow rate. Find the minimum number of steps by showing them on the graph. e) Write the equation of the operation lines of the enrichment and stripping zones. f) What is the ideal number of steps and the most suitable step position for the supply current? g) If the distillation column operates at 50% efficiency, what is the actual number of stages? h) What is the amount of ethanol transferred in the stages of the column after the full condenser and before the superheated boiler? i) What are the thermal loads (kW) of the condenser and the partial evaporation boiler? ( = 40000 kJ/kmol) please

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