Achievements:

The pyrolysis of ethane $,C_2{H}_4+O_2{C}_2{H}_{4}O$

takes place in an isobaric PBR or fluidized CSTR$.$ The feed enters at $6\mathrm{.}0$atm and $260C.$

The reactants in the feed are at a stoichiometric ratio.

What size of PBR and f$-$CSTR reactors are needed to reach $80\mathrm{.}0\%$ conversion?

$v_o=50*\frac{L}{\text{m}\text{i}\text{n}}$

$k=53\frac{\text{m}\text{o}\text{l}}{k{g}_{\text{c}\text{a}\text{t}}*min*at{m}^3}at300C$

and with respect to the limiting reagent

$E_a=80.\frac{kJ}{\text{m}\text{o}\text{l}}$