There is storage in a refinery unit where the feed is at a temperature of $80$ degrees Celsius and a pressure of $148$ psi.

Temporarily saved.

The composition of the feed in the tank includes methane, ethane, propane, normal butane, normal pentane and normal hexane and their molar composition

$0\mathrm{.}14,0\mathrm{.}27,0\mathrm{.}30,0\mathrm{.}16,0\mathrm{.}08,0\mathrm{.}02$ respectively

We want to enter this feed into a distillation tower under the pressure of the mixture, so that the product vapor at the top of the tower contains $97\mathrm{.}7\%$ propane and

$1\mathrm{.}3\%$ pentane. In this situation, calculate the following in relation to the distillery tower:

A$)$ Estimate the minimum return flow ratio and the relative composition of the products?

b$)$ Calculate the number of theoretical trays in full reverse flow and get the relative composition of the products in this state?

c$)$ If the return flow ratio is chosen equal to $0\mathrm{.}85$ get the relative composition of the products in this ratio?

d$)$ Determine the number of required trays and the location of the feed tray in the return flow ratio of $0\mathrm{.}85?$

e$)$ Determine the bubble point on the feed tray in the above two situations?

and $($calculate the heat load of condenser and boiler as well as G$/$L ratios?