protected double Source(double[] x, double[] parameters, double[] U)
{
//double Temperature = U[0] > 1.0 ? U[0] : 1.0 ;
//double YF = U[1] > 0.0 ? U[1] : 0.0;
//double YO = U[2] > 0.0 ? U[2] : 0.0;
double Temperature = U[0];
double YF = U[1];
double YO = U[2];
double Ta = ReactionRateConstants[1];
double MM_F = MolarMasses[0];
double MM_O = MolarMasses[1];
if (YF * YO > 1e-6 && VariableOneStepParameters) // calculate one-Step model parameters
{
Ta = EoS.getTa(YF, YO) / TRef;
}
rho = EoS.GetDensity(U);
double ReactionRate = m_Da * Math.Exp(-Ta / Temperature) * (rho * YF / MM_F) * (rho * YO / MM_O);
//Debug.Assert(!double.IsNaN(ReactionRate));
//Debug.Assert(!double.IsInfinity(ReactionRate));
return(-MolarMasses[SpeciesIndex] * StoichiometricCoefficients[SpeciesIndex] * ReactionRate);
}
/// <summary>
///
/// </summary>
protected double Source(double[] x, double[] parameters, double[] U)
{
rho = EoS.GetDensity(U);
Debug.Assert(!double.IsNaN(rho));
Debug.Assert(!double.IsInfinity(rho));
double Ta = ReactionRateConstants[1];
//double Temperature = U[0] > 1.0 ? U[0] : 1.0 ;
//double YF = U[1] > 0.0 ? U[1] : 0.0;
//double YO = U[2] > 0.0 ? U[2] : 0.0;
double Temperature = U[0];
double YF = U[1];
double YO = U[2];
if (YF * YO > 1e-6 && VariableOneStepParameters) // calculate one-Step model parameters
{
Ta = EoS.getTa(YF, YO) / TRef;
HeatReleaseFactor = EoS.getHeatRelease(YF, YO) / (cpRef * TRef);
}
double PM_CH4 = molarMasses[0];
double PM_O2 = molarMasses[1];
ReactionRate = m_Da * Math.Exp(-Ta / Temperature) * (rho * YF / PM_CH4) * (rho * YO / PM_O2);
return(-HeatReleaseFactor * ReactionRate * PM_CH4);
}
