Jacketed Non$-$adiabatic CSTR$.$

The reaction AlongrightarrowB takes place in a jacketed non$-$adiabatic CSTR reactor. The reaction is a single first$-$order exothermic and irreversible reaction. The reactant $A$ is converted into $b,$ the product. The initial concentration of component $A$ is $C_{Ao}=15$kmo$\frac{l}{m^3}.$ The inlet volumetric flow rate is $F_o=200\frac{m^3}{h},$ the volume of the reactor is $V=380m^3,$ the inlet temperature is $250K,$ the liquid density is $600k\frac{g}{m^3},$ and the fluid heat capacity is $C_p=3kJ(kg.K).$ Q$=1000$KW and K$=0\mathrm{.}04/$min$...$

Q$1$: Develop Degree of Freedom.

Q$2$: Derive a model that represents the given scenario.

Q$3$: Solve that problem mathematically and compare your results by SIMULINK.