solve this with graphs and drawings

An acetone$-$water solution containing $25wt\%$ acetone is to be fractionated at a rate of $10000k\frac{g}{h}r$ at $1$atm pressure, and it is planned to recover $99\mathrm{.}5\%$ of the acetone in the distillate at a concentration of $98wt\%.$ The feed will be available at $26\mathrm{.}7C$ will be preheated by heat exchanger with the residue product from the fractionator, which will in turn be cooled to $51\mathrm{.}7C.$ The distilled vapors will be condensed and cooled to $37\mathrm{.}8C$ by cooling water entering at $26\mathrm{.}7C$ and leaving at $40\mathrm{.}6C.$ Reflux will be returned at $37\mathrm{.}8C,$ at a reflux ratio $\frac{L_0}{D}=1\mathrm{.}8.$ Open steam, available at $70k\frac{N}{m^2},$ will be used at the base of the tower. The tower will be insulated to reduce heat losses to negligible values. Physical data are given below:

Use the Ponchon$-$Savarit method, and determine:

$($a$)$ The hourly rate and composition of distillate and reflux.

$($b$)$ The hourly condenser heat load and cooling water rate.

$($c$)$ The hourly rate of steam and residue and the composition of the residue.

$($d$)$ The enthalpy of the feed as it enters the tower and its condition $($express quantitatively$).$

$($e$)$ The number of theoretical trays required if the feed is introduced at the optimum location. Use large$-$size graph paper and a sharp pencil

Vapor$-$liquid equilibrium data at $1$atm, heats of solution, heat capacities, and latent heats of vaporization for the system acetone$-$water are as follows:

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