Propylene oxide $(C_3{H}_{8}O)$ is produced by reacting propylene $(C_3{H}_6)$ with oxygen and hydrogen. A side reaction results in reacting propylene with hydrogen and produces propane. A mixture of $35mo\frac{l}{h}$ air, $4mo\frac{l}{h}$ propylene, and $12\mathrm{.}6mo\frac{l}{h}$ hydrogen $(H_2)$ along with $5000mo\frac{l}{h}$ carbon dioxide is used as inert solvent$)$ is fed to a continuous reactor. The percent single$-$pass conversion of limiting reactant is $10\%.$ The fractional yield of $C_3{H}_6$ to $C_3{H}_{8}O$ is $0\mathrm{.}80($i$.$e$.,$ fraction of moles of $C_3{H}_6$ reacted to produce $C_3{H}_{8}O).$ The reactor effluents are separated where gases leave the top of the column. Propylene, propane, and propylene oxide $,$ and $($:$C_3{H}_{8}O\}$ are condensed and removed from the bottom of the column as liquids. Calculate the mole flow rate of each component in the effluent streams.

The following reactions are taking place:

$C_3{H}_6+H_2+\frac{1}{2}{O}_2{C}_3{H}_{8}O$

$C_3{H}_6+H_2{C}_3{H}_8$