Determine the heat transferred to or from the reactor to give these reactors the desired operating conditions. The answer should be given in kW$.$To calculate the specific heat capacity, follow the convention of using average temperature.Assume ideal gas conditions and that the heat capacity is independent of pressure.Draw a clearly labelled process flow diagram.Data:Heat of formation at $25\backslash$deg C and $1$ atmAH$\backslash$deg $($NH$3)=-46\mathrm{.}19$ kJ$/$mol$\backslash$deg $($NO$)=+90\mathrm{.}37$ kJ$/$mol$\backslash$deg $($HO$)=-241\mathrm{.}83$ kJ$/$mol$\backslash$deg $($N$2)=0$ kJ$/$molAH$\backslash$deg H$2)=0$ kJ$/$molHeat capacity where temperature is in $\backslash$deg CN$2$: $29\backslash$times $10-3+0\mathrm{.}2199\backslash$times $10-$ST $+0\mathrm{.}5723$ x $10-82$ kJ$/$mol$.\backslash$deg C$02$: $29\mathrm{.}1$ x $10-3+1\mathrm{.}158$ x $10-5$T $-0\mathrm{.}6076$ x $10-8$T$?$ kJ$/$mol$.\backslash$deg C NH$3$: $35\mathrm{.}15\backslash$times $10-3+2\mathrm{.}954$ x $10-5$T $+0\mathrm{.}4421\backslash$times $10-872$ kJ$/$mol$.\backslash$deg C H$20$: $33\mathrm{.}46$ x $10-3+0\mathrm{.}688$ x $10-5$T $+0\mathrm{.}7604$ x $10-8$T$?$ kJ$/$mol$.\backslash$deg CNO: $29\mathrm{.}5$ x $10-3+0\mathrm{.}8188$ x $10-$ST $-0\mathrm{.}2925$ x $10-872+0\mathrm{.}3652$ x $10-123$ kJ$/$mol$.\backslash$deg C