everything can be done in the workspace, if you do write a script or function to assist you, be sure to attach the code as a $.$txt or $.$m file.$)$

Aerobic $-a{C}_2{H}_{5}OH+bN{H}_3+c{O}_{2}longrightarrowpC{H}_{1\mathrm{.}704}{N}_{0\mathrm{.}149}{O}_{0\mathrm{.}408}+qC{O}_2+r{H}_{2}O,RQ=0\mathrm{.}66$

$[$Ethanol $+$ Ammonia $+$ Oxygen longrightarrow Biomass $+$ Carbon Dioxide $+$ Water$]$

Anaerobic $-C_6{H}_{12}{O}_6+bN{H}_3$longrightarrow$0\mathrm{.}59C{H}_{1\mathrm{.}74}{N}_{0\mathrm{.}2}{O}_{0\mathrm{.}45}+1\mathrm{.}3C_2{H}_{5}OH+q{C}_3{H}_8{O}_3+rC{O}_2+s{H}_{2}O$

$[$Glucose $+$ Ammonia longrightarrow Biomass $+$ Ethanol $+$ Ethylene Glycol $+$ Carbon Dioxide $+$ Water$]$

is scavenged out of the inlet stream$($s$)$ so that the concentration of oxygen in the reactor can be considered negligible under ideal conditions.

b$)$ Using the balanced equation for anaerobic respiration in part $($a$)$ and the information below, determine:

i$.$ the limiting reactant and fractional conversion of the other reactant

ii$.$ the mass generated of biomass and the composition of the outlet stream

iii. the final ABV if the glucose and ammonia are carried into the reactor by $16\frac{L}{h}r$ of water