The concentration of species $A$ at the inlet to the reactor $1=C_{A0}=1\mathrm{.}5mo\frac{l}{L}$

The concentration of species $B$ at the inlet to the reactor $1=C_{B0}=1\mathrm{.}5mo\frac{l}{L}$

The reactors are controlled at the desired setpoint temperature of $70C$

The specific reaction rate constant $=2\frac{L}{m}ol-hr$

$V_{PFR1}=10L,V_{PFR2}=10L$

The molar flow rate of species $A$ at the inlet to the reactor $1=F_{A0}=5mo\frac{l}{h}r$

The molar flow rate of species $B$ at the inlet to the reactor $1=F_{B0}=50mo\frac{l}{h}r$

a$.$ Determine conversion of $A$ in the first PFR $($i$.$e$.,x_{Al,PFR})?$

b$.$ What is the overall conversion of A in the second PFR in a series combination of PFRs$?$

c$.$ What would be the overall conversion if we operated the reactors in parallel?

Assume $0\mathrm{.}6v_0$ of the A and B mixture is fed to one reactor and $0\mathrm{.}4v_0$ to the second

reactor in parallel.