You are considering producing compound B by the elemental reversible reaction

in liquid phase: A $$ B $+$ C in a continuous reaction system. The diet consists

in pure A at a concentration of $5$ M$,$ a temperature of $50\backslash$deg C and a flow of $2$ mol$/$s$.$

Determine:

a$.)$ The system equilibrium conversion.

b$.)$ Make the Levenspiel graph for this system

c$.)$ It is desired to use two reactors $($a PFR and a CSTR$)$ connected in series to achieve

a total conversion of $50\%($up to $25\%$ with the first reactor and $50\%$ with the

second reactor$).$ In what order would you put the reactors $($PFR$-$CSTR or CSTRPFR$)?$ Show your proposal on the Levenspiel graph.

Additional data: k $(20\backslash$deg C$)=0\mathrm{.}0011$ L$/($s$*$kgcat$),$ Ea $=100$ kJ$/$mol$,$ KC $(50\backslash$deg C$)=5$ M$.$