MULES: Solving for alpha.fuel
Liquid phase volume fraction = 0.78646411 Min(alpha.fuel) = 0 Min(alpha.vapor) = 0
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
smoothSolver: Solving for T, Initial residual = 0.0043509939, Final residual = 5.4162916e-12, No Iterations 2
#0 Foam::error::printStack(Foam::Ostream&) at ??:?
#1 Foam::sigFpe::sigHandler(int) at ??:?
#2 ? in "/lib/x86_64-linux-gnu/libc.so.6"
#3 Foam::PengRobinsonGas<Foam::specie>::Z(double, double) const at ??:?
#4 Foam::heRhoThermo<Foam::rhoThermo, Foam::pureMixture<Foam::sutherlandTransport<Foam::species::thermo<Foam::hConstThermo<Foam::PengRobinsonGas<Foam::specie> >, Foam::sensibleEnthalpy> > > >::calculate() at ??:?
#5 Foam::heRhoThermo<Foam::rhoThermo, Foam::pureMixture<Foam::sutherlandTransport<Foam::species::thermo<Foam::hConstThermo<Foam::PengRobinsonGas<Foam::specie> >, Foam::sensibleEnthalpy> > > >::correct() at ??:?
#6 Foam::twoPhaseMixtureThermo::correct() at ??:?
#7 ? at ??:?
#8 __libc_start_main in "/lib/x86_64-linux-gnu/libc.so.6"
#9 ? at ??:?