Exercise \#3: We wish to extract a mixture of 55wt% acetone and 45wt% water with methyl isobutyl ketone (MIK) at 298K and 1 bar. If we contact 2kg of the acetone-water mixture with 3kg of pure MIK, what will be the amounts and compositions of the equilibrium phases? I have attached a ternary phase diagram for the system to use in the calculation. If you took the entire resulting water-rich phase and contacted it with another 3kg of pure MIK, what would be the final composition of each phase. Is this a feasible liquid-liquid extraction scheme? Why or why not? Please use the attached ternary diagram for your calculations