Nitric oxide $($NO$)$ can be produced by oxidizing ammonia$($NH$3)$ with oxygen $(2)$ over a catalyst. This reaction follows the stoichiometric equation:$4$ NH$,+5024$ NO $+6$H$20$The feed to the reactor consists of an equimolar mixture of NH and $02(50$ mol$\%$ NH and $50$ mol$\%02).$ Under a given set of reactor conditions, $80\%$ conversion is obtained with a fresh feed rate of $100$ mol$/$hr$.$The products of the reactor are fed to a separator which separates all the NH and O$,$ from the NO and H$20\mathrm{.}1\mathrm{.}1)$ Draw and label the flow block diagram for the process.$[2]1\mathrm{.}2)$ Show that O$,$ is the limiting reactant$\mathrm{.}1\mathrm{.}3)$ Determine the rates of production of the various species from the process$\mathrm{.}1\mathrm{.}4)$ Suppose that the recovered NH$,$ and O$,$ are recycled back to the reactor via a mixing unit. Suppose further that the fresh feed composition and conversion in the reactor is the same as before.$[3][7]1\mathrm{.}4\mathrm{.}1)$ Draw and label the flow block diagram for the modified process.$[3]1\mathrm{.}4\mathrm{.}2)$ Determine if you have enough information to calculate the production rate of NO from the process. Do not solve for the production rate of $[5]$