Given:

$k=10\mathrm{.}2$ liter $\frac{?}{(molehr)}$

$F_{Ao}=1\mathrm{.}3$mol$\frac{e}{m}in$

$V_o=2\mathrm{.}5ga\frac{l}{m}in$

$V_1=V_{CSTR}=500$gal

$V_2=V_{PFR}=400$gal

a$)$ Determine the numeric value of the Damk$$hler for the CSTR$.$

b$)$ Determine the numeric value of the Damk$$hler for the PFR$.$

c$)$ Determine the Global Conversion at the exit of the CSTR $(x_1)$ based on the feed to the first reactor.

d$)$ Determine the Global Conversion at the exit of the PFR $(x_2)$ based on the feed to the first reactor.

e$)$ Assuming we have the PFR reactor of $400$gal first, followed by the CSTR reactor of $500$gal, all other

conditions remain the same. Determine the Global Conversion at the exit of the PFR $(x_1)$ and CSTR

$(x_2)$ based on the feed to the first reactor.