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

$2D+3AC+E,r_{2K}=k_{2F}{C}_A{C}_n$

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

Additional information:

$k_{1D}=0\mathrm{.}25d\frac{m^3}{m}ol*min,{}_0=10d\frac{m^2}{m}in$

$k_{2E}=0\mathrm{.}1d\frac{m^3}{m}ol*min,C_{A0}=1\mathrm{.}5mo\frac{l}{d}{m}^3$

$k_{3y}=5\mathrm{.}0d\frac{m^6}{m}o{l}^2*min,C_{BO}=2\mathrm{.}0mo\frac{l}{d}{m}^3$

a$.$ Consider the reactions to be liquid phese and plot the species concentrations and the conversion of A as a function of the distance li$.$e$.,$ vilure$)$ down a $5U-d{m}^3$ PFR$.$ Note a$$y maxima

b$.$ Consider the reactiona to be liquid phese and detemine the effluent corcentrations and converaicn trom a $50-d{m}^3$ CSIR IAns $C_A-=0\mathrm{.}61,C_B=0\mathrm{.}79C_F=0\mathrm{.}25,$ and $C_D=0\mathrm{.}45mo\frac{l}{d}{m}^3,$

c$.$ Plot and analyze the species concentrations and the corversior of $A$ as a function of time when the reaction is corried out in a comibatoh recctor initialy contcining $40d{m}^3$ of l quid. Cono dor wo cases: $(1)A$ is fed to $B,$ and $(2)B$ is fec to $A.$ What differences do you obsen'e for these two case Describe what you find.

d$.$ Vay the rat of $B$ to Ir the feed to the PFR and descrise what you fird. What generalizotions can you mase from th $3$ problem?

e$.$ Fewark $($a$)$ for the case when the reaction is a gas$-$phase reaction. $\text{'}$Ne will keep the constants the same so you won't have to make toc many charges in your Polymsth procram, but v$/$e will make $v_0=100d\frac{m^3}{?}$ uin, $C_{Tv}=0\mathrm{.}4mo\frac{l}{d}{m}^3,V=500d{m}^3,$ and an ecuimolan leed of A and B$.$ Plot the mo ar flow rates and $S_{\frac{C}{D}}$ and $S_{\frac{B}{F}}$ down a PFR$.$ Deecribo what you find. coetficient, $k_{CD},$ can be varied setween $0\mathrm{.}1$ and $10mi{n}^{-1}.$ What trends do you find?

g$.$ Repeat $()$ whan $E$ is fed through the sidee of a memorane resctor. Describe what you find.