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fixing the running of flow_ebos_2p.

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by not adding the dummy phase.
This commit is contained in:
Kai Bao 2017-08-01 11:53:56 +02:00
parent c1ee941195
commit 6e0da756dc
1 changed files with 73 additions and 73 deletions
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146
opm/autodiff/StandardWell_impl.hpp
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@ -626,84 +626,84 @@ namespace Opm
getMobility(ebosSimulator, perf, mob);
computePerfRate(intQuants, mob, wellIndex()[perf], bhp, perfPressureDiffs()[perf], allow_cf, cq_s);
for (int componentIdx = 0; componentIdx < numComp; ++componentIdx) {
// the cq_s entering mass balance equations need to consider the efficiency factors.
const EvalWell cq_s_effective = cq_s[componentIdx] * well_efficiency_factor_;
if (!only_wells) {
// subtract sum of component fluxes in the reservoir equation.
// need to consider the efficiency factor
ebosResid[cell_idx][flowPhaseToEbosCompIdx(componentIdx)] -= cq_s_effective.value();
}
// subtract sum of phase fluxes in the well equations.
resWell_[0][componentIdx] -= cq_s[componentIdx].value();
// assemble the jacobians
for (int pvIdx = 0; pvIdx < numWellEq; ++pvIdx) {
if (!only_wells) {
// also need to consider the efficiency factor when manipulating the jacobians.
duneC_[0][cell_idx][pvIdx][flowPhaseToEbosCompIdx(componentIdx)] -= cq_s_effective.derivative(pvIdx+numEq); // intput in transformed matrix
}
invDuneD_[0][0][componentIdx][pvIdx] -= cq_s[componentIdx].derivative(pvIdx+numEq);
}
for (int pvIdx = 0; pvIdx < numEq; ++pvIdx) {
if (!only_wells) {
// also need to consider the efficiency factor when manipulating the jacobians.
ebosJac[cell_idx][cell_idx][flowPhaseToEbosCompIdx(componentIdx)][flowToEbosPvIdx(pvIdx)] -= cq_s_effective.derivative(pvIdx);
duneB_[0][cell_idx][componentIdx][flowToEbosPvIdx(pvIdx)] -= cq_s_effective.derivative(pvIdx);
}
}
// add trivial equation for 2p cases (Only support water + oil)
if (numComp == 2) {
assert(!active()[ Gas ]);
invDuneD_[0][0][Gas][Gas] = 1.0;
}
// Store the perforation phase flux for later usage.
if (has_solvent && componentIdx == contiSolventEqIdx) {// if (flowPhaseToEbosCompIdx(componentIdx) == Solvent)
well_state.perfRateSolvent()[first_perf_ + perf] = cq_s[componentIdx].value();
} else {
well_state.perfPhaseRates()[(first_perf_ + perf) * np + componentIdx] = cq_s[componentIdx].value();
}
}
if (has_polymer) {
EvalWell cq_s_poly = cq_s[Water];
if (wellType() == INJECTOR) {
cq_s_poly *= wpolymer();
} else {
cq_s_poly *= extendEval(intQuants.polymerConcentration() * intQuants.polymerViscosityCorrection());
}
if (!only_wells) {
for (int pvIdx = 0; pvIdx < numEq; ++pvIdx) {
ebosJac[cell_idx][cell_idx][contiPolymerEqIdx][flowToEbosPvIdx(pvIdx)] -= cq_s_poly.derivative(pvIdx);
}
ebosResid[cell_idx][contiPolymerEqIdx] -= cq_s_poly.value();
}
}
// Store the perforation pressure for later usage.
well_state.perfPress()[first_perf_ + perf] = well_state.bhp()[indexOfWell()] + perfPressureDiffs()[perf];
}
// add vol * dF/dt + Q to the well equations;
for (int componentIdx = 0; componentIdx < numComp; ++componentIdx) {
EvalWell resWell_loc = (wellSurfaceVolumeFraction(componentIdx) - F0_[componentIdx]) * volume / dt;
resWell_loc += getQs(componentIdx);
for (int pvIdx = 0; pvIdx < numWellEq; ++pvIdx) {
invDuneD_[0][0][componentIdx][pvIdx] += resWell_loc.derivative(pvIdx+numEq);
}
resWell_[0][componentIdx] += resWell_loc.value();
// the cq_s entering mass balance equations need to consider the efficiency factors.
const EvalWell cq_s_effective = cq_s[componentIdx] * well_efficiency_factor_;
// add trivial equation for polymer
if (has_polymer) {
invDuneD_[0][0][contiPolymerEqIdx][polymerConcentrationIdx] = 1.0;
if (!only_wells) {
// subtract sum of component fluxes in the reservoir equation.
// need to consider the efficiency factor
ebosResid[cell_idx][flowPhaseToEbosCompIdx(componentIdx)] -= cq_s_effective.value();
}
// subtract sum of phase fluxes in the well equations.
resWell_[0][componentIdx] -= cq_s[componentIdx].value();
// assemble the jacobians
for (int pvIdx = 0; pvIdx < numWellEq; ++pvIdx) {
if (!only_wells) {
// also need to consider the efficiency factor when manipulating the jacobians.
duneC_[0][cell_idx][pvIdx][flowPhaseToEbosCompIdx(componentIdx)] -= cq_s_effective.derivative(pvIdx+numEq); // intput in transformed matrix
}
invDuneD_[0][0][componentIdx][pvIdx] -= cq_s[componentIdx].derivative(pvIdx+numEq);
}
for (int pvIdx = 0; pvIdx < numEq; ++pvIdx) {
if (!only_wells) {
// also need to consider the efficiency factor when manipulating the jacobians.
ebosJac[cell_idx][cell_idx][flowPhaseToEbosCompIdx(componentIdx)][flowToEbosPvIdx(pvIdx)] -= cq_s_effective.derivative(pvIdx);
duneB_[0][cell_idx][componentIdx][flowToEbosPvIdx(pvIdx)] -= cq_s_effective.derivative(pvIdx);
}
}
// add a trivial equation for the dummy phase for 2p cases (Only support water + oil)
if ( numComp < numWellEq ) {
assert(!active()[ Gas ]);
invDuneD_[0][0][Gas][Gas] = 1.0;
}
// Store the perforation phase flux for later usage.
if (has_solvent && componentIdx == contiSolventEqIdx) {// if (flowPhaseToEbosCompIdx(componentIdx) == Solvent)
well_state.perfRateSolvent()[first_perf_ + perf] = cq_s[componentIdx].value();
} else {
well_state.perfPhaseRates()[(first_perf_ + perf) * np + componentIdx] = cq_s[componentIdx].value();
}
}
if (has_polymer) {
EvalWell cq_s_poly = cq_s[Water];
if (wellType() == INJECTOR) {
cq_s_poly *= wpolymer();
} else {
cq_s_poly *= extendEval(intQuants.polymerConcentration() * intQuants.polymerViscosityCorrection());
}
if (!only_wells) {
for (int pvIdx = 0; pvIdx < numEq; ++pvIdx) {
ebosJac[cell_idx][cell_idx][contiPolymerEqIdx][flowToEbosPvIdx(pvIdx)] -= cq_s_poly.derivative(pvIdx);
}
ebosResid[cell_idx][contiPolymerEqIdx] -= cq_s_poly.value();
}
}
// Store the perforation pressure for later usage.
well_state.perfPress()[first_perf_ + perf] = well_state.bhp()[indexOfWell()] + perfPressureDiffs()[perf];
}
// add vol * dF/dt + Q to the well equations;
for (int componentIdx = 0; componentIdx < numComp; ++componentIdx) {
EvalWell resWell_loc = (wellSurfaceVolumeFraction(componentIdx) - F0_[componentIdx]) * volume / dt;
resWell_loc += getQs(componentIdx);
for (int pvIdx = 0; pvIdx < numWellEq; ++pvIdx) {
invDuneD_[0][0][componentIdx][pvIdx] += resWell_loc.derivative(pvIdx+numEq);
}
resWell_[0][componentIdx] += resWell_loc.value();
// add trivial equation for polymer
if (has_polymer) {
invDuneD_[0][0][contiPolymerEqIdx][polymerConcentrationIdx] = 1.0;
}
}
// do the local inversion of D.
localInvert( invDuneD_ );
}