Problem $2(5$ points$)$

The aqueous phase decomposition of species A takes place according to the equation $AR$ and follows second order reaction kinetics with a rate constant $k=1$ liter$/($mole$*$ min. Because of an existing PFR reactor in the $p$ run this decomt, a recent Chemical Engineer graduate uses this PFR reactor, which has a volume of $70$ liters, to this PFR reactor is $1$ reaction of A isothermally and with no pressure drop. The concentration of A fed to His boss, an experis $1$mol$\frac{e}{?}$ liter, while its molar flow rate to this reactor is $15$mol$\frac{e}{m}in.$ CSTR decides to $2$ exists with a volume twice of that of the PFR$.$ The process engineer responsible for this by treating his CSalculate how much the molar flow rate of the product $R$ at the output of the CSTR will be with molar flow CSTR as independent $($stand$-$alone reactor$)$ that has an input stream which contains A and R molar flow flow rates equal to the molar flow rates of A and $R$ in the output of the PFR reactor. What is the reactors ate of product $R$ this process engineer has calculated? Note that both the PFR and the CSTR