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Under specific conditions, some reaction rate expressions are dependent on pressure and temperature. This is especially true for the rate associated to unimolecular/recombination fall-off reactions which increases with pressure. In such cases, if the chemical process takes place in a high or low pressure limit | Under specific conditions, some reaction rate expressions are dependent on pressure and temperature. This is especially true for the rate associated to unimolecular/recombination fall-off reactions which increases with pressure. In such cases, if the chemical process takes place in a high or low pressure limit | ||
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<reaction reversible="yes" type="falloff" id="0012"> | <reaction reversible="yes" type="falloff" id="0012"> | ||
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=== Reaction rates === | === Reaction rates === |
Revision as of 16:32, 7 March 2016
Contents
Chemical kinetics
This chapter reports the principles that drive the computation of combustion chemistry in most CFD softwares.
Chemkin (.scheme .therm .trans), Cantera (xml)
...
Arrhenius law
is the pre-exponential factor, is the temperature exponent and the activation energy
Three-body reactions
In the forward direction, three-body reactions involve two species A and B as reactants and yield a single product AB. In that case, the third body M is used to stabilize the excited product AB*. On the contrary, in the reverse direction, heat provides the energy necessary to break the link between A and B.
The third body M can be any inert molecule.
Falloff reactions
Under specific conditions, some reaction rate expressions are dependent on pressure and temperature. This is especially true for the rate associated to unimolecular/recombination fall-off reactions which increases with pressure. In such cases, if the chemical process takes place in a high or low pressure limit
<!-- reaction 0012 -->
<reaction reversible="yes" type="falloff" id="0012">
<equation>O + CO (+ M) [=] CO2 (+ M)</equation>
<rateCoeff>
<Arrhenius>
<A>1.800000E+07</A>
<b>0</b>
<E units="cal/mol">2385.000000</E>
</Arrhenius>
<Arrhenius name="k0">
<A>6.020000E+08</A>
<b>0</b>
<E units="cal/mol">3000.000000</E>
</Arrhenius>
<efficiencies default="1.0">AR:0.5 C2H6:3 CH4:2 CO:1.5 CO2:3.5 H2:2 H2O:6 O2:6 </efficiencies>
<falloff type="Lindemann"/>
</rateCoeff>
<reactants>CO:1 O:1.0</reactants>
<products>CO2:1.0</products>
</reaction>
</code>
=== Reaction rates ===
The global rate of a reaction j (evolution in concentration per unit of time) varies depending on the proportion of the rates associated to the forward and backward directions.
<math>
\mathcal{Q}_j = \mathcal{Q}_{f,j} - \mathcal{Q}_{r,j}
</math>
=== Production/Consumption source terms ===
Species <math>Y_k</math> source terms are deduced from
<math>
\dot{\omega}_k = W_k \sum_{j=1}^{N_R} \nu_{k,j} \mathcal{Q}_j
</math>
== Solver to build reference trajectories ==
== DRGEP solver for species reduction ==
* Compute species direct inter-relations
* Compute species relations through indirect paths
* Compute relations between targets and
== DRGEP solver for reactions reduction ==
== QSS solver ==
* Solve for thermodynamic
<math>h_k = \Delta h_{f,k}^{0} + h_{sk}</math>
<math>h_{sk} = \int_{T_0}^{T} Cp_k dT</math>
Get Gibbs Free Energy
Get Equilibrium constants