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Add comments to the well equations
Gas and solvent is combinded and solved together The input in the well equation is then the total gas phase = hydro carbon gas + solvent gas This may need to be reconsidered later, as the model is tested.
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@ -269,9 +269,16 @@ namespace Opm {
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int gas_pos = fluid_.phaseUsage().phase_pos[Gas];
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int oil_pos = fluid_.phaseUsage().phase_pos[Oil];
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// remove contribution from the dissolved gas.
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// TODO compensate for gas in the oil phase
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assert(!has_vapoil_);
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const ADB cq_s_solvent = wellSolventFraction * (cq_s[gas_pos] - rs_perfcells * cq_s[oil_pos]);
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//cq_s[gas_pos] = ( ones - wellSolventFraction ) * cq_s[gas_pos];;
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// Solvent contribution to the mass balance equation is given as a fraction
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// of the gas contribution.
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residual_.material_balance_eq[solvent_pos_] -= superset(cq_s_solvent, well_cells, nc);
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// The gas contribution must be reduced accordingly for the total contribution to be
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// the same.
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residual_.material_balance_eq[gas_pos] += superset(cq_s_solvent, well_cells, nc);
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}
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@ -463,9 +470,14 @@ namespace Opm {
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}
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if (has_solvent_) {
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int gas_pos = fluid_.phaseUsage().phase_pos[Gas];
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// Gas and solvent is combinded and solved together
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// The input in the well equation is then the
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// total gas phase = hydro carbon gas + solvent gas
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// This may need to be reconsidered later, as the model
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// is tested.
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mob_perfcells[gas_pos] += subset(rq_[solvent_pos_].mob, well_cells);
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b_perfcells[gas_pos] += subset(rq_[solvent_pos_].b, well_cells);
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}
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if (param_.solve_welleq_initially_ && initial_assembly) {
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// solve the well equations as a pre-processing step
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