P$3-12$a in this problem, the complex reactions described below will first be carried out in the linuid phase $($parts $($a$)$ through $($d$))$ and then in the gas phase $($parts $($e$)$ through $($g$)).$ One need not solve the liquid phase to solve the ges$-$phase problems.

The follcwing reactions are carried out iscthermally.

$A+2BC+D,r_{10}=k_{1D}{C}_A{C}_n$

$2D+3AC+E,r_{3F}=k_1{C}_4{C}_n$

$B+2CD+F,r_{3}F=k_{2F}{C}_B^2{C}_C$

Additional information:

$A_{1D}=0\mathrm{.}25d\frac{m^3}{m}ol-$min,${}_0=10d\frac{m^3}{m}in$

$A_{zE}=0\mathrm{.}1d\frac{m^3}{m}ol*min,C_{Ma}=1\mathrm{.}5mo\frac{l}{d}{m}^3$

$ksy=5\mathrm{.}0d\frac{m^4}{m}o{l}^2*min,C_{be}=2\mathrm{.}0mo\frac{l}{d}{m}^3$

a$.$ Consider the reactons to be licuid phess and pict the species concentrations and the conversion of A as a function of the sistance $($i$.$e$.,$ vure$)$ down a $5U-d{m}^3$ PFR$.$ Note ayy mavima

b$.$ Consider the reactions to be licuid phese and detemine the efluent corcentrations and conversicn

c$.$ Flot and analye the species concentrations and the corversior of $A$ as a function of time when the reaction ie corriod out in a comibatsh recctor intial y contcining $40d{m}^2$ of louic. Coro dor vo Cates: $(1)A$ is fed to $B$ and $(2)B$ is fec to $A.$ What amerences de you obsenve tor thesa Rwo cases? Describe wat you find.

d$.$ Vay the rat of $B$ to ir the feed to the PFR and describe what vou tirc. What goseraizationa can you mace from th a problom?