please help me with 1-9 if possible using Beard, Marianna J numbers !

please number each problem you work out and write clear! thank you so much for your help.

A continuous, steady-state distillation column with a total condenser and a partial reboilet separates methanol from water at one atmosphere total pressure. The feed rate to the column is Fib-mole hour and the feed temperature is maintained at T C The feed contains mw mass % methanol and wwf mass t water. A distillate product contains mwD mass % methanol and a bottoms product contains mm mole methanol. The external reflux tato Disd. Wa F moler Feed Temperature T, Methanol ma the food mw Melanoma in the distillate Meth mole is the hote pod the feed K.C. Kwon Beard, Marianna J. Brantley. Leah P. Garrett, Jayla E Harden, Brianna K. Harry, Ibiada M. Humphrey, Robyn R. Jones, Omario Jordan, Michael W. Miller, Krysta N. Norwood, Justin D Price, Tyshell. Williams, Kalyce 1 862 534.7 518.5 4651 784.8 691.4 760.9 408.1 829.3 559.6 391.5 5313 346.5 24 26.12 30.65 35.04 29.73 36.78 29.63 38.56 32.45 30.92 27 82 26.86 26.65 25 38.03 3621 33.49 37.64 3146 37.76 34.28 31.17 29.95 28.9 29.23 26.61 74 61.97 63.79 66.51 62.36 68.54 62.24 65.72 68.83 70.05 71.1 70.77 73.39 88.35 95 69 86.39 75.86 97.62 94 86 98.62 925 81.01 78.38 96.33 89.13 90.44 27 3.50 4.48 3.41 4.31 332 268 4.19 422 275 3.15 3.66 3.10 3.2 3.51 284 2.65 3.65 3.04 3.89 3.48 3.75 4.04 3.88 3.19 2.55 1. Sketch the problem according to the description of the problem. 2. Find the mean heat capacity (cal/g-molo-K) of the distillate stream over the temperature range of T (the feed temperature) - To the distillate condensation) temperature). 3. Find the mean beat capacity (calg-mole-K) of the bottom product stream over the temperature range of T (the feed temperature) - T. (the bottom product temperature) 4. Find the specific enthalpy hr (cal/g-mole) of the feed stream, using the feed temperature Tras a reference temperature 5. Find the specific enthalpy ho (cal/g-mole) of the distillate stream, using the food temperature Trasa reference temperature 6. Find the specific enthalpy ha (cal/g-mole) of the bottom product strcam, using the feed temperature Tras a reference temperature. 7. Calculate the latent heat of vaporization (cal/g-mole) for the vapor stream at the distillate (condensation) temperature To, using Watson's correlation, shown below. 23 2 latent heat of vaporization at TK ts= Relatent heat of vaporization at TK T. critical temperature, K Calculate the heat duty of the total condenser in callhe. Calculate the heat duty of the reboiler in cal/har. latent heat of vaporization for Watson's Method Liquid heat capacities THE C al T. T."K C1.987 (calg-mole-K) (13.431-5.1280x10 T1.311310) kjgmole 1987 (call-molo-K) (8.712 +1.2500x10 T-1800010 1 methanol 35.27 513.20 2 water 40.656 8 9. 100 6474 Tin K Vapor-liquid equilibrium data (Table 2-7) for the methanol-water system at 1 atm. ZE XE 0 0.02 0.04 0.06 0.08 01 0.15 0.2 03 0.4 0.5 0.6 0.7 0.8 09 0.95 1 TC 100 96.4 93.5 91.2 893 1877 84.4 81.7 78 M VE 0 0134 0.23 0.304 0.165 0418 0.517 0.579 0.665 0.729 0.779 0.25 0.87 0.915 0.958 0.979 1 W T 253 73.1 71.2 693 67,6 66 65 645