```{py:currentmodule} cantera ``` # Ideal Gas Constant Pressure Mole Reactor An ideal gas constant pressure mole reactor, as implemented by the C++ class {ct}`IdealGasConstPressureMoleReactor` and available in Python as the {py:class}`IdealGasConstPressureMoleReactor` class. It is defined by the state variables: - $T$, the temperature (in K) - $n_k$, the number of moles for each species (in kmol) Equations 1 and 2 below are the governing equations for an ideal gas constant pressure mole reactor. ## Species Equations The moles of each species in the reactor changes as a result of flow through the reactor's [inlets and outlets](sec-flow-device), and production of homogeneous gas phase species and reactions on the reactor [surfaces](sec-reactor-surface). The rate at which species $k$ is generated through homogeneous phase reactions is $V \dot{\omega}_k$, and the total rate at which moles of species $k$ changes is: $$ \frac{dn_k}{dt} = V \dot{\omega}_k + \sum_\t{in} \dot{n}_{k, \t{in}} - \sum_\t{out} \dot{n}_{k, \t{out}} + \dot{n}_{k, \t{wall}} $$ (ig-const-pressure-mole-reactor-species) Where the subscripts *in* and *out* refer to the sum of the corresponding property over all inlets and outlets respectively. A dot above a variable signifies a time derivative. ## Energy Equation Writing the first law for an open system gives: $$ \frac{dU}{dt} = - p \frac{dV}{dt} + \dot{Q} + \sum_\t{in} \dot{n}_\t{in} \hat{h}_\t{in} - \hat{h} \sum_\t{out} \dot{n}_\t{out} $$ where positive $\dot{Q}$ represents heat addition to the system and $h$ is the specific enthalpy of the reactor's contents. Differentiating the definition of the total enthalpy, $H = U + pV$, with respect to time gives: $$ \frac{dH}{dt} = \frac{dU}{dt} + p \frac{dV}{dt} + V \frac{dp}{dt} $$ Noting that $dp/dt = 0$ and substituting into the energy equation yields: $$ \frac{dH}{dt} = \dot{Q} + \sum_\t{in} \dot{n}_\t{in} \hat{h}_\t{in} - \hat{h} \sum_\t{out} \dot{n}_\t{out} $$ As for the [ideal gas mole reactor](ideal-gas-mole-reactor), we replace the total enthalpy as a state variable with the temperature by writing the total enthalpy in terms of the species moles and temperature: $$ H = \sum_k \hat{h}_k(T) n_k $$ and differentiating with respect to time: $$ \frac{dH}{dt} = \frac{dT}{dt}\sum_k n_k \hat{c}_{p,k} + \sum \hat{h}_k \dot{n}_k $$ Making this substitution and rearranging yields an equation for the temperature: $$ \sum_k n_k \hat{c}_{p,k} \frac{dT}{dt} = \dot{Q} - \sum \hat{h}_k \dot{n}_k $$ (ig-const-pressure-mole-reactor-energy)