A liquid phase first order exothermic chemical reaction $AB,$ is taking place in three continuously stirred tank reactors in series with constant liquid volumes $V_1,V_2$ and $V_3.$ The reaction rate constant in the reactors are different and are $k_1,k_2$ and $k_3,$ respectively. The flow rate, temperature and concentration $($of component A$)$ of the inlet stream to the first reactor are $F_0(\frac{m^3}{m}in),T_0(C)$ and $C_{A0}(\frac{\text{m}\text{o}\text{l}}{m^3}),$ respectively.

Initially, concentration of $A$ in the first tank is $C_{Ai}(mo\frac{l}{m^3})$ while other tanks do not contain any $A.$ All the tanks are initially at temperature $T_i.$ Heat is removed from the reactors via coiled coils at rates of $Q_1,Q_2$ and $Q_3(\frac{J}{m}in),$ respectively. You can assume constant heat capacities, liquid densities and heat of reaction. Using the data in the table below:

$\backslash$table$[[T_0=25C,F_0=2\mathrm{.}5\frac{m^3}{m}in,C_{A0}=1\mathrm{.}8mo\frac{l}{m^3}$