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6fe856136d
to allow iteration over the energy equations to improve stability for phase-change. Additionally if nEnergyCorrectors is set to 0 the energy equations are not solved which may be beneficial during the startup of some cases.
65 lines
1.4 KiB
C
65 lines
1.4 KiB
C
for (int Ecorr=0; Ecorr<nEnergyCorrectors; Ecorr++)
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{
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fluid.correctEnergyTransport();
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autoPtr<phaseSystem::heatTransferTable>
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heatTransferPtr(fluid.heatTransfer());
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phaseSystem::heatTransferTable&
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heatTransfer = heatTransferPtr();
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{
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tmp<fvScalarMatrix> E1Eqn(phase1.heEqn());
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if (E1Eqn.valid())
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{
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E1Eqn =
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(
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E1Eqn
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==
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*heatTransfer[phase1.name()]
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+ alpha1*rho1*(U1&g)
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+ fvOptions(alpha1, rho1, phase1.thermo().he())
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);
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E1Eqn->relax();
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fvOptions.constrain(E1Eqn());
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E1Eqn->solve();
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}
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}
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{
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tmp<fvScalarMatrix> E2eqn(phase2.heEqn());
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if (E2eqn.valid())
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{
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E2eqn =
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(
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E2eqn
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==
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*heatTransfer[phase2.name()]
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+ alpha2*rho2*(U2&g)
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+ fvOptions(alpha2, rho2, phase2.thermo().he())
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);
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E2eqn->relax();
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fvOptions.constrain(E2eqn());
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E2eqn->solve();
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}
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}
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}
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fluid.correctThermo();
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Info<< phase1.name() << " min/max T "
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<< min(phase1.thermo().T()).value()
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<< " - "
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<< max(phase1.thermo().T()).value()
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<< endl;
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Info<< phase2.name() << " min/max T "
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<< min(phase2.thermo().T()).value()
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<< " - "
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<< max(phase2.thermo().T()).value()
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<< endl;
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