solve the problem using aspen plus and show $($screenshots$)$ each steps of your aspen code:

P$11-6$ The irreversible endothermic vapor$-$phase reaction follows an elementary rate law ${?}_B$

$C{H}_{3}COC{H}_{3}C{H}_{2}CO+C{H}_4$

$AB+C$

and is carried out adiabatically in a $500-d{m}^{3}PFR.$ Species A is fed to the reactor at a rate of $10mo\frac{l}{m}in$

and a pressure of $2$atm. An inert stream is also fed to the reactor at $2$atm, as shown in Figure P$11-C_B.$

The entrance temperature of both streams is $1100K.$

F

Additional information:

$k=$exp$(34\mathrm{.}34-34,\frac{222}{T})d\frac{m^3}{m}ol*min,C_{P_{\text{I}}}=200\frac{J}{m}ol*K$

$(Tin$ degrees Kelvin $),$

$C_{P_A}=170\frac{J}{m}ol*K,C_{P_B}=90\frac{J}{m}ol*K$

$C_{P_C}=80\frac{J}{m}ol*K,H_{Rx}=80,000\frac{J}{m}ol$

$($a$)$ First derive an expression for $C_{A01}$ as a function of $C_{A0}$ and ${}_{\text{I}}.$

$($b$)$ Sketch the conversion and temperature profiles for the case when no inerts are present. Using a

dashed line, sketch the profiles when a moderate amount of inerts are added. Using a dotted line,

sketch the profiles when a large amount of inerts are added. Qualitative sketches are fine. Describe

the similarities and differences between the curves.

$($c$)$ Sketch or plot and then analyze the exit conversion as a function of ${}_{\text{I}}.$ Is there a ratio of the

entering molar flow rates of inerts $($I$)$ to A $($i$.$e$.,{}_{\text{I}}=\frac{F_{I0}}{F_{A0}})$ at which the conversion is at a

maximum? Explain why there $"$is$"$ or $"$is not" a maximum.

$($d$)$ What would change in parts $($b$)$ and $($c$)$ if reactions were exothermic and reversible with

$H_{Rx}=-80k\frac{J}{m}ol$ and $K_C=2d\frac{m^3}{m}ol$ at $1100K?$

$($e$)$ Sketch or plot $F_B$ for parts $($c$)$ and $($d$),$ and describe what you find.

$($f$)$ Plot the heat that must be removed along the reactor $(Q^{}$ vs$.V)$ to maintain isothermal operation

for pure A fed and an exothermic reaction. Part $($f$)$ is $"$C$"$ level of difficulty, i$.$e$.,$ P$11-6C_C(f).$