In a continuously operated non$-$isothermal cylindrical stirred tank reactor there is one

chemical reaction takes place. The following information is available about the system:

Reactor inlet temperature: $350$ K $($const$.)$

Temperature of the heating bath: $360$ K $($const$.)$

Adiabatic temperature increase: $45$ K $($const$.)$

Density of the reaction mixture: $0\mathrm{.}8$ g$/$ml $($const$.)$

Heat capacity of the reaction mixture: $2\mathrm{.}3$ J g$-1$ K$-1($const$.)$

Heat transfer coefficient Kw: $500$ W m$-2$ K$-1($const$.)$

Reaction volume $=$ reactor volume $=1$m$3$

$($const$.)$

Volume flow: $1340$ L h$-1($const$.)$

Diameter $=$ reactor height $($heat exchange via base, cover and jacket of the cylinder$)$

Determine the operating point graphically using the enclosed heat generation curve.