Write steps $1-3$ of the algorithm on paper. Also, write your formulas for the specified yield and

selectivity quantities.

Use Polymath to combine and evaluate and generate plots for the quantities specified. Organize your

Polymath reports and plots into a single document $($Word recommended$).$

A set of complex gas$-$phase reactions are shown below. Each reaction follows an elementary rates law.

$A+\frac{1}{2}B{k}_{1}C,k_1=0\mathrm{.}014\frac{(\frac{L}{m}ol{)}^{0\mathrm{.}5}}{s}$

$2A{k}_{2}D,k_2=0\mathrm{.}007\frac{L}{m}o\frac{l}{s}$

$C{k}_{3}E+W,k_3=\frac{0\mathrm{.}014}{s}$

$W+D{k}_{4}G+C,k_4=0\mathrm{.}45\frac{L}{m}o\frac{l}{s}$

The entering flow rates are $F_{A0}=10mo\frac{l}{s},F_{B0}=5mo\frac{l}{s},$ and $v_0=100\frac{L}{s}.$ At a total entering concentration

$C_{T0}=0\mathrm{.}15mo\frac{l}{L},$ consider a reactor volume of $V=200,000L.$

Plot the molar flow rates of each species along the volume $($length$)$ of the reactor on the same figure. Then

separately plot each of the following along the length of the reactor: tilde$(Y{)}_C,$tilde$(S{)}_{\frac{A}{E}},$tilde$(S{)}_{\frac{C}{D}},$tilde$(S{)}_{\frac{D}{G}}$Write steps $1-3$ of the algorithm on paper. Also, write your formulas for the specified yield and selectivity quantities. Use Polymath to combine and evaluate and generate plots for the quantities specified. Organize your Polymath reports and plots into a single document $($Word recommended$).$ A set of complex gas$-$phase reactions are shown below. Each reaction follows an elementary rates law. A$+(1)/(2)$B$->$k$\_(1)$C$,$k$\_(1)=0\mathrm{.}014((($L$)/($m$)$ol$)^(0\mathrm{.}5))/($s$)2$A$->$k$\_(2)$D$,$k$\_(2)=0\mathrm{.}007($L$)/($m$)$o$($l$)/($s$)$ C$->$k$\_(3)$E$+$W$,$k$\_(3)=(0\mathrm{.}014)/($s$)$ W$+$D$->$k$\_(4)$G$+$C$,$k$\_(4)=0\mathrm{.}45($L$)/($m$)$o$($l$)/($s$)$ The entering flow rates are F$\_($A$0)=10$mo$($l$)/($s$),$F$\_($B$0)=5$mo$($l$)/($s$),$ and v$\_(0)=100($L$)/($s$).$ At a total entering concentration C$\_($T$0)=0\mathrm{.}15$mo$($l$)/($L$),$ consider a reactor volume of V$=200,000$L $.$ Plot the molar flow rates of each species along the volume $($length$)$ of the reactor on the same figure. Then separately plot each of the following along the length of the reactor: tilde$($Y$)\_($C$),$tilde$($S$)\_(($A$)/($E$)),$tilde$($S$)\_(($C$)/($D$)),$tilde$($S$)\_(($D$)/($G$))$