In a continuously operated non$-$isothermal cylindrical stirred tank reactor, a chemical reaction occurs. The following information is available for the system:

$-$ Reactor inlet temperature: $350$ K $($constant$)$

$-$ Temperature of the heat bath: $360$ K $($constant$)$

$-$ Adiabatic temperature increase: $45$ K $($constant$)$

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

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

$-$ Heat transfer coefficient Kw: $500$ W$$m$^-2$K$^-1($constant$)$

$-$ Reaction volume $=$ Reactor volume $=1$m$^3($constant$)$

$-$ Volumetric flow rate: $1340$ L$$h$^-1($constant$)$

$-$ Diameter $=$ Reactor height $($Heat exchange over bottom, lid, and jacket of the cylinder$)$

Determine the operating point graphically with the accompanying heat generation curve.