c$)$ The following second$-$order reaction A$-$Products is cartied out in a tubutar reactor. The kinetic constant is $k=0\mathrm{.}1\frac{m^2}{k}$mol.$s$ and the reaction occurs im liquid phase. The reactor is $L=30m$ long and has a diameter of $D=4cm.$ The inlet mixture is pure $A$ at conceritration $C_{A_0}=10$kmo$\frac{l}{m^3}$ and is Colodity is $v=8\mathrm{.}1\frac{m}{s}.$ The Residence Time Distribution function was expedmentaly measured and reported incthe table below $($closed$/$closed boundary conditions can be assumed$).$

$($i$)$ Estimate the Peclet number and the effective dispersion$/$coefficient according to

Co the Dispersion Model.

$($ii$)$ Estimate the number of equivalent CSTR according to the Tanks$-$in$-$Series model and the corresponding outlet concentration and cobversion of A$.$ Make a comparison with the ideal plug flow reactor