2021-06-03 08:34:14 -05:00
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/*
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Copyright 2017 SINTEF Digital, Mathematics and Cybernetics.
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Copyright 2017 Statoil ASA.
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This file is part of the Open Porous Media project (OPM).
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OPM is free software: you can redistribute it and/or modify
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it under the terms of the GNU General Public License as published by
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the Free Software Foundation, either version 3 of the License, or
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(at your option) any later version.
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OPM is distributed in the hope that it will be useful,
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but WITHOUT ANY WARRANTY; without even the implied warranty of
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MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE. See the
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GNU General Public License for more details.
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You should have received a copy of the GNU General Public License
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along with OPM. If not, see <http://www.gnu.org/licenses/>.
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*/
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#include <config.h>
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2022-10-18 11:21:11 -05:00
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2021-06-03 08:34:14 -05:00
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#include <opm/simulators/wells/MultisegmentWellEval.hpp>
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2022-08-29 08:59:28 -05:00
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#include <dune/istl/umfpack.hh>
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2021-06-03 08:34:14 -05:00
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#include <opm/material/fluidsystems/BlackOilFluidSystem.hpp>
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#include <opm/models/blackoil/blackoilindices.hh>
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#include <opm/models/blackoil/blackoilonephaseindices.hh>
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#include <opm/models/blackoil/blackoiltwophaseindices.hh>
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#include <opm/simulators/timestepping/ConvergenceReport.hpp>
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#include <opm/simulators/utils/DeferredLoggingErrorHelpers.hpp>
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#include <opm/simulators/wells/MSWellHelpers.hpp>
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#include <opm/simulators/wells/MultisegmentWellAssemble.hpp>
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2022-10-31 10:03:59 -05:00
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#include <opm/simulators/wells/WellAssemble.hpp>
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#include <opm/simulators/wells/WellConvergence.hpp>
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#include <opm/simulators/wells/WellInterfaceIndices.hpp>
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#include <opm/simulators/wells/WellState.hpp>
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2022-10-18 11:21:11 -05:00
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#include <algorithm>
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#include <array>
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#include <cassert>
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#include <cmath>
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#include <numeric>
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#include <utility>
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#include <vector>
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namespace Opm
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{
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template<typename FluidSystem, typename Indices, typename Scalar>
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MultisegmentWellEval<FluidSystem,Indices,Scalar>::
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MultisegmentWellEval(WellInterfaceIndices<FluidSystem,Indices,Scalar>& baseif)
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: MultisegmentWellGeneric<Scalar>(baseif)
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, baseif_(baseif)
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, linSys_(*this)
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, primary_variables_(baseif)
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, segments_(this->numberOfSegments(), baseif)
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, cell_perforation_depth_diffs_(baseif_.numPerfs(), 0.0)
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, cell_perforation_pressure_diffs_(baseif_.numPerfs(), 0.0)
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{
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}
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template<typename FluidSystem, typename Indices, typename Scalar>
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void
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MultisegmentWellEval<FluidSystem,Indices,Scalar>::
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initMatrixAndVectors(const int num_cells)
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{
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linSys_.init(num_cells, baseif_.numPerfs(),
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baseif_.cells(), segments_.inlets_,
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segments_.perforations_);
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primary_variables_.resize(this->numberOfSegments());
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}
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template<typename FluidSystem, typename Indices, typename Scalar>
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ConvergenceReport
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MultisegmentWellEval<FluidSystem,Indices,Scalar>::
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getWellConvergence(const WellState& well_state,
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const std::vector<double>& B_avg,
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DeferredLogger& deferred_logger,
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const double max_residual_allowed,
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const double tolerance_wells,
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const double relaxed_inner_tolerance_flow_ms_well,
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const double tolerance_pressure_ms_wells,
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const double relaxed_inner_tolerance_pressure_ms_well,
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const bool relax_tolerance) const
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{
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assert(int(B_avg.size()) == baseif_.numComponents());
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// checking if any residual is NaN or too large. The two large one is only handled for the well flux
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std::vector<std::vector<double>> abs_residual(this->numberOfSegments(),
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std::vector<double>(numWellEq, 0.0));
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for (int seg = 0; seg < this->numberOfSegments(); ++seg) {
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for (int eq_idx = 0; eq_idx < numWellEq; ++eq_idx) {
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abs_residual[seg][eq_idx] = std::abs(linSys_.residual()[seg][eq_idx]);
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}
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}
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std::vector<double> maximum_residual(numWellEq, 0.0);
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ConvergenceReport report;
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// TODO: the following is a little complicated, maybe can be simplified in some way?
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for (int eq_idx = 0; eq_idx < numWellEq; ++eq_idx) {
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for (int seg = 0; seg < this->numberOfSegments(); ++seg) {
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if (eq_idx < baseif_.numComponents()) { // phase or component mass equations
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const double flux_residual = B_avg[eq_idx] * abs_residual[seg][eq_idx];
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if (flux_residual > maximum_residual[eq_idx]) {
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maximum_residual[eq_idx] = flux_residual;
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}
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} else { // pressure or control equation
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// for the top segment (seg == 0), it is control equation, will be checked later separately
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if (seg > 0) {
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// Pressure equation
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const double pressure_residual = abs_residual[seg][eq_idx];
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if (pressure_residual > maximum_residual[eq_idx]) {
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maximum_residual[eq_idx] = pressure_residual;
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}
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}
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}
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}
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}
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using CR = ConvergenceReport;
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for (int eq_idx = 0; eq_idx < numWellEq; ++eq_idx) {
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if (eq_idx < baseif_.numComponents()) { // phase or component mass equations
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const double flux_residual = maximum_residual[eq_idx];
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// TODO: the report can not handle the segment number yet.
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if (std::isnan(flux_residual)) {
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report.setWellFailed({CR::WellFailure::Type::MassBalance, CR::Severity::NotANumber, eq_idx, baseif_.name()});
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} else if (flux_residual > max_residual_allowed) {
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report.setWellFailed({CR::WellFailure::Type::MassBalance, CR::Severity::TooLarge, eq_idx, baseif_.name()});
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} else if (!relax_tolerance && flux_residual > tolerance_wells) {
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report.setWellFailed({CR::WellFailure::Type::MassBalance, CR::Severity::Normal, eq_idx, baseif_.name()});
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} else if (flux_residual > relaxed_inner_tolerance_flow_ms_well) {
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report.setWellFailed({CR::WellFailure::Type::MassBalance, CR::Severity::Normal, eq_idx, baseif_.name()});
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}
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} else { // pressure equation
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const double pressure_residual = maximum_residual[eq_idx];
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const int dummy_component = -1;
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if (std::isnan(pressure_residual)) {
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report.setWellFailed({CR::WellFailure::Type::Pressure, CR::Severity::NotANumber, dummy_component, baseif_.name()});
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} else if (std::isinf(pressure_residual)) {
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report.setWellFailed({CR::WellFailure::Type::Pressure, CR::Severity::TooLarge, dummy_component, baseif_.name()});
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} else if (!relax_tolerance && pressure_residual > tolerance_pressure_ms_wells) {
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report.setWellFailed({CR::WellFailure::Type::Pressure, CR::Severity::Normal, dummy_component, baseif_.name()});
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} else if (pressure_residual > relaxed_inner_tolerance_pressure_ms_well) {
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report.setWellFailed({CR::WellFailure::Type::Pressure, CR::Severity::Normal, dummy_component, baseif_.name()});
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}
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}
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}
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2022-10-27 03:43:44 -05:00
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WellConvergence(baseif_).
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checkConvergenceControlEq(well_state,
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{tolerance_pressure_ms_wells,
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tolerance_pressure_ms_wells,
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tolerance_wells,
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tolerance_wells,
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max_residual_allowed},
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std::abs(linSys_.residual()[0][SPres]),
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report,
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deferred_logger);
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return report;
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}
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template<typename FluidSystem, typename Indices, typename Scalar>
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typename MultisegmentWellEval<FluidSystem,Indices,Scalar>::EvalWell
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MultisegmentWellEval<FluidSystem,Indices,Scalar>::
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extendEval(const Eval& in) const
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{
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EvalWell out = 0.0;
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out.setValue(in.value());
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for(int eq_idx = 0; eq_idx < Indices::numEq;++eq_idx) {
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out.setDerivative(eq_idx, in.derivative(eq_idx));
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}
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return out;
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}
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template<typename FluidSystem, typename Indices, typename Scalar>
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typename MultisegmentWellEval<FluidSystem,Indices,Scalar>::EvalWell
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MultisegmentWellEval<FluidSystem,Indices,Scalar>::
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getFrictionPressureLoss(const int seg) const
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{
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const EvalWell mass_rate = segments_.mass_rates_[seg];
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const int seg_upwind = segments_.upwinding_segments_[seg];
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EvalWell density = segments_.densities_[seg_upwind];
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EvalWell visc = segments_.viscosities_[seg_upwind];
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// WARNING
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// We disregard the derivatives from the upwind density to make sure derivatives
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// wrt. to different segments dont get mixed.
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if (seg != seg_upwind) {
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density.clearDerivatives();
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visc.clearDerivatives();
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}
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const int outlet_segment_index = this->segmentNumberToIndex(this->segmentSet()[seg].outletSegment());
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const double length = this->segmentSet()[seg].totalLength() - this->segmentSet()[outlet_segment_index].totalLength();
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assert(length > 0.);
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const double roughness = this->segmentSet()[seg].roughness();
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const double area = this->segmentSet()[seg].crossArea();
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const double diameter = this->segmentSet()[seg].internalDiameter();
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const double sign = mass_rate < 0. ? 1.0 : - 1.0;
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return sign * mswellhelpers::frictionPressureLoss(length, diameter, area, roughness, density, mass_rate, visc);
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}
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template<typename FluidSystem, typename Indices, typename Scalar>
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typename MultisegmentWellEval<FluidSystem,Indices,Scalar>::EvalWell
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MultisegmentWellEval<FluidSystem,Indices,Scalar>::
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pressureDropSpiralICD(const int seg) const
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{
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const SICD& sicd = this->segmentSet()[seg].spiralICD();
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const int seg_upwind = segments_.upwinding_segments_[seg];
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const std::vector<EvalWell>& phase_fractions = segments_.phase_fractions_[seg_upwind];
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const std::vector<EvalWell>& phase_viscosities = segments_.phase_viscosities_[seg_upwind];
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EvalWell water_fraction = 0.;
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EvalWell water_viscosity = 0.;
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if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
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const int water_pos = Indices::canonicalToActiveComponentIndex(FluidSystem::waterCompIdx);
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water_fraction = phase_fractions[water_pos];
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water_viscosity = phase_viscosities[water_pos];
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}
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EvalWell oil_fraction = 0.;
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EvalWell oil_viscosity = 0.;
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if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
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const int oil_pos = Indices::canonicalToActiveComponentIndex(FluidSystem::oilCompIdx);
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oil_fraction = phase_fractions[oil_pos];
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oil_viscosity = phase_viscosities[oil_pos];
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}
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EvalWell gas_fraction = 0.;
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EvalWell gas_viscosity = 0.;
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if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
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const int gas_pos = Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx);
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gas_fraction = phase_fractions[gas_pos];
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gas_viscosity = phase_viscosities[gas_pos];
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}
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EvalWell density = segments_.densities_[seg_upwind];
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// WARNING
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// We disregard the derivatives from the upwind density to make sure derivatives
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// wrt. to different segments dont get mixed.
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if (seg != seg_upwind) {
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water_fraction.clearDerivatives();
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water_viscosity.clearDerivatives();
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oil_fraction.clearDerivatives();
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oil_viscosity.clearDerivatives();
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gas_fraction.clearDerivatives();
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gas_viscosity.clearDerivatives();
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density.clearDerivatives();
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}
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2022-11-17 08:20:56 -06:00
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const EvalWell liquid_fraction = water_fraction + oil_fraction;
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// viscosity contribution from the liquid
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const EvalWell liquid_viscosity_fraction = liquid_fraction < 1.e-30 ? oil_fraction * oil_viscosity + water_fraction * water_viscosity :
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liquid_fraction * mswellhelpers::emulsionViscosity(water_fraction, water_viscosity, oil_fraction, oil_viscosity, sicd);
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const EvalWell mixture_viscosity = liquid_viscosity_fraction + gas_fraction * gas_viscosity;
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const EvalWell reservoir_rate = segments_.mass_rates_[seg] / density;
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const EvalWell reservoir_rate_icd = reservoir_rate * sicd.scalingFactor();
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const double viscosity_cali = sicd.viscosityCalibration();
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using MathTool = MathToolbox<EvalWell>;
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const double density_cali = sicd.densityCalibration();
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const EvalWell temp_value1 = MathTool::pow(density / density_cali, 0.75);
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const EvalWell temp_value2 = MathTool::pow(mixture_viscosity / viscosity_cali, 0.25);
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// formulation before 2016, base_strength is used
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// const double base_strength = sicd.strength() / density_cali;
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// formulation since 2016, strength is used instead
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const double strength = sicd.strength();
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const double sign = reservoir_rate_icd <= 0. ? 1.0 : -1.0;
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return sign * temp_value1 * temp_value2 * strength * reservoir_rate_icd * reservoir_rate_icd;
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}
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template<typename FluidSystem, typename Indices, typename Scalar>
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typename MultisegmentWellEval<FluidSystem,Indices,Scalar>::EvalWell
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MultisegmentWellEval<FluidSystem,Indices,Scalar>::
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pressureDropAutoICD(const int seg,
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const UnitSystem& unit_system) const
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{
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const AutoICD& aicd = this->segmentSet()[seg].autoICD();
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2022-12-19 06:05:07 -06:00
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const int seg_upwind = segments_.upwinding_segments_[seg];
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const std::vector<EvalWell>& phase_fractions = this->segments_.phase_fractions_[seg_upwind];
|
|
|
|
const std::vector<EvalWell>& phase_viscosities = this->segments_.phase_viscosities_[seg_upwind];
|
|
|
|
const std::vector<EvalWell>& phase_densities = this->segments_.phase_densities_[seg_upwind];
|
2021-06-03 08:34:14 -05:00
|
|
|
|
|
|
|
EvalWell water_fraction = 0.;
|
|
|
|
EvalWell water_viscosity = 0.;
|
|
|
|
EvalWell water_density = 0.;
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
|
|
const int water_pos = Indices::canonicalToActiveComponentIndex(FluidSystem::waterCompIdx);
|
|
|
|
water_fraction = phase_fractions[water_pos];
|
|
|
|
water_viscosity = phase_viscosities[water_pos];
|
|
|
|
water_density = phase_densities[water_pos];
|
|
|
|
}
|
|
|
|
|
|
|
|
EvalWell oil_fraction = 0.;
|
|
|
|
EvalWell oil_viscosity = 0.;
|
|
|
|
EvalWell oil_density = 0.;
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
|
|
|
|
const int oil_pos = Indices::canonicalToActiveComponentIndex(FluidSystem::oilCompIdx);
|
|
|
|
oil_fraction = phase_fractions[oil_pos];
|
|
|
|
oil_viscosity = phase_viscosities[oil_pos];
|
|
|
|
oil_density = phase_densities[oil_pos];
|
|
|
|
}
|
|
|
|
|
|
|
|
EvalWell gas_fraction = 0.;
|
|
|
|
EvalWell gas_viscosity = 0.;
|
|
|
|
EvalWell gas_density = 0.;
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
|
|
const int gas_pos = Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx);
|
|
|
|
gas_fraction = phase_fractions[gas_pos];
|
|
|
|
gas_viscosity = phase_viscosities[gas_pos];
|
|
|
|
gas_density = phase_densities[gas_pos];
|
|
|
|
}
|
|
|
|
|
2022-12-19 06:05:07 -06:00
|
|
|
EvalWell density = segments_.densities_[seg_upwind];
|
2021-06-03 08:34:14 -05:00
|
|
|
// WARNING
|
|
|
|
// We disregard the derivatives from the upwind density to make sure derivatives
|
|
|
|
// wrt. to different segments dont get mixed.
|
|
|
|
if (seg != seg_upwind) {
|
|
|
|
water_fraction.clearDerivatives();
|
|
|
|
water_viscosity.clearDerivatives();
|
|
|
|
water_density.clearDerivatives();
|
|
|
|
oil_fraction.clearDerivatives();
|
|
|
|
oil_viscosity.clearDerivatives();
|
|
|
|
oil_density.clearDerivatives();
|
|
|
|
gas_fraction.clearDerivatives();
|
|
|
|
gas_viscosity.clearDerivatives();
|
|
|
|
gas_density.clearDerivatives();
|
|
|
|
density.clearDerivatives();
|
|
|
|
}
|
|
|
|
|
|
|
|
using MathTool = MathToolbox<EvalWell>;
|
|
|
|
const EvalWell mixture_viscosity = MathTool::pow(water_fraction, aicd.waterViscExponent()) * water_viscosity
|
|
|
|
+ MathTool::pow(oil_fraction, aicd.oilViscExponent()) * oil_viscosity
|
|
|
|
+ MathTool::pow(gas_fraction, aicd.gasViscExponent()) * gas_viscosity;
|
|
|
|
|
|
|
|
const EvalWell mixture_density = MathTool::pow(water_fraction, aicd.waterDensityExponent()) * water_density
|
|
|
|
+ MathTool::pow(oil_fraction, aicd.oilDensityExponent()) * oil_density
|
|
|
|
+ MathTool::pow(gas_fraction, aicd.gasDensityExponent()) * gas_density;
|
|
|
|
|
|
|
|
const double rho_reference = aicd.densityCalibration();
|
|
|
|
const double visc_reference = aicd.viscosityCalibration();
|
2022-12-19 06:05:07 -06:00
|
|
|
const auto volume_rate_icd = this->segments_.mass_rates_[seg] * aicd.scalingFactor() / mixture_density;
|
2021-06-03 08:34:14 -05:00
|
|
|
const double sign = volume_rate_icd <= 0. ? 1.0 : -1.0;
|
|
|
|
// convert 1 unit volume rate
|
|
|
|
using M = UnitSystem::measure;
|
|
|
|
const double unit_volume_rate = unit_system.to_si(M::geometric_volume_rate, 1.);
|
|
|
|
|
|
|
|
// TODO: we did not consider the maximum allowed rate here
|
|
|
|
const auto result = sign / rho_reference * mixture_density * mixture_density
|
|
|
|
* MathTool::pow(visc_reference/mixture_viscosity, aicd.viscExponent())
|
|
|
|
* aicd.strength() * MathTool::pow( -sign * volume_rate_icd, aicd.flowRateExponent())
|
|
|
|
* std::pow(unit_volume_rate, (2. - aicd.flowRateExponent())) ;
|
|
|
|
return result;
|
|
|
|
}
|
|
|
|
|
|
|
|
template<typename FluidSystem, typename Indices, typename Scalar>
|
|
|
|
typename MultisegmentWellEval<FluidSystem,Indices,Scalar>::EvalWell
|
|
|
|
MultisegmentWellEval<FluidSystem,Indices,Scalar>::
|
|
|
|
pressureDropValve(const int seg) const
|
|
|
|
{
|
|
|
|
const Valve& valve = this->segmentSet()[seg].valve();
|
|
|
|
|
2022-12-19 06:05:07 -06:00
|
|
|
const EvalWell& mass_rate = segments_.mass_rates_[seg];
|
|
|
|
const int seg_upwind = segments_.upwinding_segments_[seg];
|
|
|
|
EvalWell visc = segments_.viscosities_[seg_upwind];
|
|
|
|
EvalWell density = segments_.densities_[seg_upwind];
|
2021-06-03 08:34:14 -05:00
|
|
|
// WARNING
|
|
|
|
// We disregard the derivatives from the upwind density to make sure derivatives
|
|
|
|
// wrt. to different segments dont get mixed.
|
|
|
|
if (seg != seg_upwind) {
|
|
|
|
visc.clearDerivatives();
|
|
|
|
density.clearDerivatives();
|
|
|
|
}
|
|
|
|
|
|
|
|
const double additional_length = valve.pipeAdditionalLength();
|
|
|
|
const double roughness = valve.pipeRoughness();
|
|
|
|
const double diameter = valve.pipeDiameter();
|
|
|
|
const double area = valve.pipeCrossArea();
|
|
|
|
|
|
|
|
const EvalWell friction_pressure_loss =
|
|
|
|
mswellhelpers::frictionPressureLoss(additional_length, diameter, area, roughness, density, mass_rate, visc);
|
|
|
|
|
|
|
|
const double area_con = valve.conCrossArea();
|
|
|
|
const double cv = valve.conFlowCoefficient();
|
|
|
|
|
|
|
|
const EvalWell constriction_pressure_loss =
|
|
|
|
mswellhelpers::valveContrictionPressureLoss(mass_rate, density, area_con, cv);
|
|
|
|
|
|
|
|
const double sign = mass_rate <= 0. ? 1.0 : -1.0;
|
|
|
|
return sign * (friction_pressure_loss + constriction_pressure_loss);
|
|
|
|
}
|
|
|
|
|
|
|
|
template<typename FluidSystem, typename Indices, typename Scalar>
|
|
|
|
void
|
|
|
|
MultisegmentWellEval<FluidSystem,Indices,Scalar>::
|
|
|
|
handleAccelerationPressureLoss(const int seg,
|
2022-11-30 16:06:44 -06:00
|
|
|
WellState& well_state)
|
2021-06-03 08:34:14 -05:00
|
|
|
{
|
|
|
|
const double area = this->segmentSet()[seg].crossArea();
|
2022-12-19 06:05:07 -06:00
|
|
|
const EvalWell mass_rate = segments_.mass_rates_[seg];
|
|
|
|
const int seg_upwind = segments_.upwinding_segments_[seg];
|
|
|
|
EvalWell density = segments_.densities_[seg_upwind];
|
2021-06-03 08:34:14 -05:00
|
|
|
// WARNING
|
|
|
|
// We disregard the derivatives from the upwind density to make sure derivatives
|
|
|
|
// wrt. to different segments dont get mixed.
|
|
|
|
if (seg != seg_upwind) {
|
|
|
|
density.clearDerivatives();
|
|
|
|
}
|
|
|
|
|
|
|
|
EvalWell accelerationPressureLoss = mswellhelpers::velocityHead(area, mass_rate, density);
|
|
|
|
// handling the velocity head of intlet segments
|
2022-12-19 06:52:21 -06:00
|
|
|
for (const int inlet : this->segments_.inlets_[seg]) {
|
2022-12-19 06:05:07 -06:00
|
|
|
const int seg_upwind_inlet = segments_.upwinding_segments_[inlet];
|
2021-06-03 08:34:14 -05:00
|
|
|
const double inlet_area = this->segmentSet()[inlet].crossArea();
|
2022-12-19 06:05:07 -06:00
|
|
|
EvalWell inlet_density = this->segments_.densities_[seg_upwind_inlet];
|
2021-06-03 08:34:14 -05:00
|
|
|
// WARNING
|
|
|
|
// We disregard the derivatives from the upwind density to make sure derivatives
|
|
|
|
// wrt. to different segments dont get mixed.
|
|
|
|
if (inlet != seg_upwind_inlet) {
|
|
|
|
inlet_density.clearDerivatives();
|
|
|
|
}
|
2022-12-19 06:05:07 -06:00
|
|
|
const EvalWell inlet_mass_rate = segments_.mass_rates_[inlet];
|
2021-06-03 08:34:14 -05:00
|
|
|
accelerationPressureLoss -= mswellhelpers::velocityHead(std::max(inlet_area, area), inlet_mass_rate, inlet_density);
|
|
|
|
}
|
|
|
|
|
|
|
|
// We change the sign of the accelerationPressureLoss for injectors.
|
|
|
|
// Is this correct? Testing indicates that this is what the reference simulator does
|
|
|
|
const double sign = mass_rate < 0. ? 1.0 : - 1.0;
|
|
|
|
accelerationPressureLoss *= sign;
|
|
|
|
|
2021-08-05 05:55:18 -05:00
|
|
|
auto& segments = well_state.well(baseif_.indexOfWell()).segments;
|
|
|
|
segments.pressure_drop_accel[seg] = accelerationPressureLoss.value();
|
2021-06-03 08:34:14 -05:00
|
|
|
|
2022-11-18 05:09:43 -06:00
|
|
|
MultisegmentWellAssemble<FluidSystem,Indices,Scalar>(baseif_).
|
|
|
|
assemblePressureLoss(seg, seg_upwind, accelerationPressureLoss, linSys_);
|
2021-06-03 08:34:14 -05:00
|
|
|
}
|
|
|
|
|
|
|
|
template<typename FluidSystem, typename Indices, typename Scalar>
|
|
|
|
void
|
|
|
|
MultisegmentWellEval<FluidSystem,Indices,Scalar>::
|
|
|
|
assembleDefaultPressureEq(const int seg,
|
2022-11-30 16:06:44 -06:00
|
|
|
WellState& well_state)
|
2021-06-03 08:34:14 -05:00
|
|
|
{
|
|
|
|
assert(seg != 0); // not top segment
|
|
|
|
|
|
|
|
// for top segment, the well control equation will be used.
|
2022-12-19 02:52:48 -06:00
|
|
|
EvalWell pressure_equation = primary_variables_.getSegmentPressure(seg);
|
2021-06-03 08:34:14 -05:00
|
|
|
|
|
|
|
// we need to handle the pressure difference between the two segments
|
|
|
|
// we only consider the hydrostatic pressure loss first
|
|
|
|
// TODO: we might be able to add member variables to store these values, then we update well state
|
|
|
|
// after converged
|
2022-12-19 07:20:55 -06:00
|
|
|
const auto hydro_pressure_drop = segments_.getHydroPressureLoss(seg);
|
2021-08-05 05:55:18 -05:00
|
|
|
auto& ws = well_state.well(baseif_.indexOfWell());
|
|
|
|
auto& segments = ws.segments;
|
2021-06-03 08:34:14 -05:00
|
|
|
segments.pressure_drop_hydrostatic[seg] = hydro_pressure_drop.value();
|
|
|
|
pressure_equation -= hydro_pressure_drop;
|
|
|
|
|
|
|
|
if (this->frictionalPressureLossConsidered()) {
|
|
|
|
const auto friction_pressure_drop = getFrictionPressureLoss(seg);
|
|
|
|
pressure_equation -= friction_pressure_drop;
|
|
|
|
segments.pressure_drop_friction[seg] = friction_pressure_drop.value();
|
|
|
|
}
|
|
|
|
|
|
|
|
// contribution from the outlet segment
|
|
|
|
const int outlet_segment_index = this->segmentNumberToIndex(this->segmentSet()[seg].outletSegment());
|
2022-12-19 02:52:48 -06:00
|
|
|
const EvalWell outlet_pressure = primary_variables_.getSegmentPressure(outlet_segment_index);
|
2021-06-03 08:34:14 -05:00
|
|
|
|
2022-12-19 06:05:07 -06:00
|
|
|
const int seg_upwind = segments_.upwinding_segments_[seg];
|
2022-11-18 05:09:43 -06:00
|
|
|
MultisegmentWellAssemble<FluidSystem,Indices,Scalar>(baseif_).
|
|
|
|
assemblePressureEq(seg, seg_upwind, outlet_segment_index,
|
|
|
|
pressure_equation, outlet_pressure, linSys_);
|
2021-06-03 08:34:14 -05:00
|
|
|
|
|
|
|
if (this->accelerationalPressureLossConsidered()) {
|
|
|
|
handleAccelerationPressureLoss(seg, well_state);
|
|
|
|
}
|
|
|
|
}
|
|
|
|
|
|
|
|
template<typename FluidSystem, typename Indices, typename Scalar>
|
|
|
|
void
|
|
|
|
MultisegmentWellEval<FluidSystem,Indices,Scalar>::
|
|
|
|
assembleICDPressureEq(const int seg,
|
|
|
|
const UnitSystem& unit_system,
|
|
|
|
WellState& well_state,
|
2022-11-30 16:06:44 -06:00
|
|
|
DeferredLogger& deferred_logger)
|
2021-06-03 08:34:14 -05:00
|
|
|
{
|
|
|
|
// TODO: upwinding needs to be taken care of
|
|
|
|
// top segment can not be a spiral ICD device
|
|
|
|
assert(seg != 0);
|
|
|
|
|
2022-06-29 07:20:35 -05:00
|
|
|
if (const auto& segment = this->segmentSet()[seg];
|
|
|
|
(segment.segmentType() == Segment::SegmentType::VALVE) &&
|
|
|
|
(segment.valve().status() == Opm::ICDStatus::SHUT) ) { // we use a zero rate equation to handle SHUT valve
|
2022-11-18 05:09:43 -06:00
|
|
|
MultisegmentWellAssemble<FluidSystem,Indices,Scalar>(baseif_).
|
2022-11-09 05:26:46 -06:00
|
|
|
assembleTrivialEq(seg, this->primary_variables_.eval(seg)[WQTotal].value(), linSys_);
|
2022-06-29 07:20:35 -05:00
|
|
|
|
|
|
|
auto& ws = well_state.well(baseif_.indexOfWell());
|
|
|
|
ws.segments.pressure_drop_friction[seg] = 0.;
|
|
|
|
return;
|
2022-06-29 04:54:36 -05:00
|
|
|
}
|
|
|
|
|
2021-06-03 08:34:14 -05:00
|
|
|
// the pressure equation is something like
|
|
|
|
// p_seg - deltaP - p_outlet = 0.
|
|
|
|
// the major part is how to calculate the deltaP
|
|
|
|
|
2022-12-19 02:52:48 -06:00
|
|
|
EvalWell pressure_equation = primary_variables_.getSegmentPressure(seg);
|
2021-06-03 08:34:14 -05:00
|
|
|
|
|
|
|
EvalWell icd_pressure_drop;
|
|
|
|
switch(this->segmentSet()[seg].segmentType()) {
|
|
|
|
case Segment::SegmentType::SICD :
|
|
|
|
icd_pressure_drop = pressureDropSpiralICD(seg);
|
|
|
|
break;
|
|
|
|
case Segment::SegmentType::AICD :
|
|
|
|
icd_pressure_drop = pressureDropAutoICD(seg, unit_system);
|
|
|
|
break;
|
|
|
|
case Segment::SegmentType::VALVE :
|
|
|
|
icd_pressure_drop = pressureDropValve(seg);
|
|
|
|
break;
|
|
|
|
default: {
|
|
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Segment " + std::to_string(this->segmentSet()[seg].segmentNumber())
|
|
|
|
+ " for well " + baseif_.name() + " is not of ICD type", deferred_logger);
|
|
|
|
}
|
|
|
|
}
|
|
|
|
pressure_equation = pressure_equation - icd_pressure_drop;
|
2021-08-05 05:55:18 -05:00
|
|
|
auto& ws = well_state.well(baseif_.indexOfWell());
|
|
|
|
ws.segments.pressure_drop_friction[seg] = icd_pressure_drop.value();
|
2021-06-03 08:34:14 -05:00
|
|
|
|
|
|
|
// contribution from the outlet segment
|
|
|
|
const int outlet_segment_index = this->segmentNumberToIndex(this->segmentSet()[seg].outletSegment());
|
2022-12-19 02:52:48 -06:00
|
|
|
const EvalWell outlet_pressure = primary_variables_.getSegmentPressure(outlet_segment_index);
|
2021-06-03 08:34:14 -05:00
|
|
|
|
2022-12-19 06:05:07 -06:00
|
|
|
const int seg_upwind = segments_.upwinding_segments_[seg];
|
2022-11-18 05:09:43 -06:00
|
|
|
MultisegmentWellAssemble<FluidSystem,Indices,Scalar>(baseif_).
|
|
|
|
assemblePressureEq(seg, seg_upwind, outlet_segment_index,
|
|
|
|
pressure_equation, outlet_pressure,
|
|
|
|
linSys_,
|
|
|
|
FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx),
|
|
|
|
FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx));
|
2021-06-03 08:34:14 -05:00
|
|
|
}
|
|
|
|
|
|
|
|
template<typename FluidSystem, typename Indices, typename Scalar>
|
|
|
|
void
|
|
|
|
MultisegmentWellEval<FluidSystem,Indices,Scalar>::
|
|
|
|
assemblePressureEq(const int seg,
|
|
|
|
const UnitSystem& unit_system,
|
|
|
|
WellState& well_state,
|
2022-11-30 16:06:44 -06:00
|
|
|
DeferredLogger& deferred_logger)
|
2021-06-03 08:34:14 -05:00
|
|
|
{
|
|
|
|
switch(this->segmentSet()[seg].segmentType()) {
|
|
|
|
case Segment::SegmentType::SICD :
|
|
|
|
case Segment::SegmentType::AICD :
|
|
|
|
case Segment::SegmentType::VALVE : {
|
|
|
|
assembleICDPressureEq(seg, unit_system, well_state,deferred_logger);
|
|
|
|
break;
|
|
|
|
}
|
|
|
|
default :
|
|
|
|
assembleDefaultPressureEq(seg, well_state);
|
|
|
|
}
|
|
|
|
}
|
|
|
|
|
|
|
|
template<typename FluidSystem, typename Indices, typename Scalar>
|
2022-04-08 04:07:34 -05:00
|
|
|
std::pair<bool, std::vector<Scalar> >
|
2021-06-03 08:34:14 -05:00
|
|
|
MultisegmentWellEval<FluidSystem,Indices,Scalar>::
|
2022-04-08 04:07:34 -05:00
|
|
|
getFiniteWellResiduals(const std::vector<Scalar>& B_avg,
|
|
|
|
DeferredLogger& deferred_logger) const
|
2021-06-03 08:34:14 -05:00
|
|
|
{
|
|
|
|
assert(int(B_avg.size() ) == baseif_.numComponents());
|
|
|
|
std::vector<Scalar> residuals(numWellEq + 1, 0.0);
|
|
|
|
|
|
|
|
for (int seg = 0; seg < this->numberOfSegments(); ++seg) {
|
|
|
|
for (int eq_idx = 0; eq_idx < numWellEq; ++eq_idx) {
|
|
|
|
double residual = 0.;
|
|
|
|
if (eq_idx < baseif_.numComponents()) {
|
2022-11-18 05:59:16 -06:00
|
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|
residual = std::abs(linSys_.residual()[seg][eq_idx]) * B_avg[eq_idx];
|
2021-06-03 08:34:14 -05:00
|
|
|
} else {
|
|
|
|
if (seg > 0) {
|
2022-11-18 05:59:16 -06:00
|
|
|
residual = std::abs(linSys_.residual()[seg][eq_idx]);
|
2021-06-03 08:34:14 -05:00
|
|
|
}
|
|
|
|
}
|
|
|
|
if (std::isnan(residual) || std::isinf(residual)) {
|
2022-04-08 04:07:34 -05:00
|
|
|
deferred_logger.debug("nan or inf value for residal get for well " + baseif_.name()
|
|
|
|
+ " segment " + std::to_string(seg) + " eq_idx " + std::to_string(eq_idx));
|
|
|
|
return {false, residuals};
|
2021-06-03 08:34:14 -05:00
|
|
|
}
|
|
|
|
|
|
|
|
if (residual > residuals[eq_idx]) {
|
|
|
|
residuals[eq_idx] = residual;
|
|
|
|
}
|
|
|
|
}
|
|
|
|
}
|
|
|
|
|
|
|
|
// handling the control equation residual
|
|
|
|
{
|
2022-11-18 05:59:16 -06:00
|
|
|
const double control_residual = std::abs(linSys_.residual()[0][numWellEq - 1]);
|
2021-06-03 08:34:14 -05:00
|
|
|
if (std::isnan(control_residual) || std::isinf(control_residual)) {
|
2022-04-08 04:07:34 -05:00
|
|
|
deferred_logger.debug("nan or inf value for control residal get for well " + baseif_.name());
|
|
|
|
return {false, residuals};
|
2021-06-03 08:34:14 -05:00
|
|
|
}
|
|
|
|
residuals[numWellEq] = control_residual;
|
|
|
|
}
|
|
|
|
|
2022-04-08 04:07:34 -05:00
|
|
|
return {true, residuals};
|
2021-06-03 08:34:14 -05:00
|
|
|
}
|
|
|
|
|
|
|
|
template<typename FluidSystem, typename Indices, typename Scalar>
|
|
|
|
double
|
|
|
|
MultisegmentWellEval<FluidSystem,Indices,Scalar>::
|
|
|
|
getControlTolerance(const WellState& well_state,
|
|
|
|
const double tolerance_wells,
|
|
|
|
const double tolerance_pressure_ms_wells,
|
|
|
|
DeferredLogger& deferred_logger) const
|
|
|
|
{
|
|
|
|
double control_tolerance = 0.;
|
|
|
|
|
|
|
|
const int well_index = baseif_.indexOfWell();
|
2021-08-04 05:03:36 -05:00
|
|
|
const auto& ws = well_state.well(well_index);
|
2021-06-03 08:34:14 -05:00
|
|
|
if (baseif_.isInjector() )
|
|
|
|
{
|
2021-08-04 05:03:36 -05:00
|
|
|
auto current = ws.injection_cmode;
|
2021-06-03 08:34:14 -05:00
|
|
|
switch(current) {
|
|
|
|
case Well::InjectorCMode::THP:
|
|
|
|
control_tolerance = tolerance_pressure_ms_wells;
|
|
|
|
break;
|
|
|
|
case Well::InjectorCMode::BHP:
|
|
|
|
control_tolerance = tolerance_wells;
|
|
|
|
break;
|
|
|
|
case Well::InjectorCMode::RATE:
|
|
|
|
case Well::InjectorCMode::RESV:
|
|
|
|
control_tolerance = tolerance_wells;
|
|
|
|
break;
|
|
|
|
case Well::InjectorCMode::GRUP:
|
|
|
|
control_tolerance = tolerance_wells;
|
|
|
|
break;
|
|
|
|
default:
|
|
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Unknown well control control types for well " << baseif_.name(), deferred_logger);
|
|
|
|
}
|
|
|
|
}
|
|
|
|
|
|
|
|
if (baseif_.isProducer() )
|
|
|
|
{
|
2021-08-04 05:03:36 -05:00
|
|
|
auto current = ws.production_cmode;
|
2021-06-03 08:34:14 -05:00
|
|
|
switch(current) {
|
|
|
|
case Well::ProducerCMode::THP:
|
|
|
|
control_tolerance = tolerance_pressure_ms_wells; // 0.1 bar
|
|
|
|
break;
|
|
|
|
case Well::ProducerCMode::BHP:
|
|
|
|
control_tolerance = tolerance_wells; // 0.01 bar
|
|
|
|
break;
|
|
|
|
case Well::ProducerCMode::ORAT:
|
|
|
|
case Well::ProducerCMode::WRAT:
|
|
|
|
case Well::ProducerCMode::GRAT:
|
|
|
|
case Well::ProducerCMode::LRAT:
|
|
|
|
case Well::ProducerCMode::RESV:
|
|
|
|
case Well::ProducerCMode::CRAT:
|
|
|
|
control_tolerance = tolerance_wells; // smaller tolerance for rate control
|
|
|
|
break;
|
|
|
|
case Well::ProducerCMode::GRUP:
|
|
|
|
control_tolerance = tolerance_wells; // smaller tolerance for rate control
|
|
|
|
break;
|
|
|
|
default:
|
|
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Unknown well control control types for well " << baseif_.name(), deferred_logger);
|
|
|
|
}
|
|
|
|
}
|
|
|
|
|
|
|
|
return control_tolerance;
|
|
|
|
}
|
|
|
|
|
|
|
|
template<typename FluidSystem, typename Indices, typename Scalar>
|
|
|
|
double
|
|
|
|
MultisegmentWellEval<FluidSystem,Indices,Scalar>::
|
|
|
|
getResidualMeasureValue(const WellState& well_state,
|
|
|
|
const std::vector<double>& residuals,
|
|
|
|
const double tolerance_wells,
|
|
|
|
const double tolerance_pressure_ms_wells,
|
|
|
|
DeferredLogger& deferred_logger) const
|
|
|
|
{
|
|
|
|
assert(int(residuals.size()) == numWellEq + 1);
|
|
|
|
|
|
|
|
const double rate_tolerance = tolerance_wells;
|
|
|
|
int count = 0;
|
|
|
|
double sum = 0;
|
|
|
|
for (int eq_idx = 0; eq_idx < numWellEq - 1; ++eq_idx) {
|
|
|
|
if (residuals[eq_idx] > rate_tolerance) {
|
|
|
|
sum += residuals[eq_idx] / rate_tolerance;
|
|
|
|
++count;
|
|
|
|
}
|
|
|
|
}
|
|
|
|
|
|
|
|
const double pressure_tolerance = tolerance_pressure_ms_wells;
|
|
|
|
if (residuals[SPres] > pressure_tolerance) {
|
|
|
|
sum += residuals[SPres] / pressure_tolerance;
|
|
|
|
++count;
|
|
|
|
}
|
|
|
|
|
|
|
|
const double control_tolerance = getControlTolerance(well_state,
|
|
|
|
tolerance_wells,
|
|
|
|
tolerance_pressure_ms_wells,
|
|
|
|
deferred_logger);
|
|
|
|
if (residuals[SPres + 1] > control_tolerance) {
|
|
|
|
sum += residuals[SPres + 1] / control_tolerance;
|
|
|
|
++count;
|
|
|
|
}
|
|
|
|
|
|
|
|
// if (count == 0), it should be converged.
|
|
|
|
assert(count != 0);
|
|
|
|
|
|
|
|
return sum;
|
|
|
|
}
|
|
|
|
|
2022-11-10 13:24:21 -06:00
|
|
|
#define INSTANCE(...) \
|
|
|
|
template class MultisegmentWellEval<BlackOilFluidSystem<double,BlackOilDefaultIndexTraits>,__VA_ARGS__,double>;
|
2021-06-03 08:34:14 -05:00
|
|
|
|
|
|
|
// One phase
|
2022-11-10 13:24:21 -06:00
|
|
|
INSTANCE(BlackOilOnePhaseIndices<0u,0u,0u,0u,false,false,0u,1u,0u>)
|
|
|
|
INSTANCE(BlackOilOnePhaseIndices<0u,0u,0u,1u,false,false,0u,1u,0u>)
|
|
|
|
INSTANCE(BlackOilOnePhaseIndices<0u,0u,0u,0u,false,false,0u,1u,5u>)
|
2021-06-03 08:34:14 -05:00
|
|
|
|
|
|
|
// Two phase
|
2022-11-10 13:24:21 -06:00
|
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,0u,0u,false,false,0u,0u,0u>)
|
|
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,0u,0u,false,false,0u,1u,0u>)
|
|
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,0u,0u,false,false,0u,2u,0u>)
|
|
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,0u,0u,false,true,0u,2u,0u>)
|
|
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,1u,0u,false,false,0u,2u,0u>)
|
|
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,2u,0u,false,false,0u,2u,0u>)
|
|
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,0u,1u,false,false,0u,1u,0u>)
|
|
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,0u,0u,false,true,0u,0u,0u>)
|
2021-06-03 08:34:14 -05:00
|
|
|
|
|
|
|
// Blackoil
|
2022-11-10 13:24:21 -06:00
|
|
|
INSTANCE(BlackOilIndices<0u,0u,0u,0u,false,false,0u,0u>)
|
|
|
|
INSTANCE(BlackOilIndices<0u,0u,0u,0u,true,false,0u,0u>)
|
|
|
|
INSTANCE(BlackOilIndices<0u,0u,0u,0u,false,true,0u,0u>)
|
|
|
|
INSTANCE(BlackOilIndices<0u,0u,0u,0u,false,true,2u,0u>)
|
|
|
|
INSTANCE(BlackOilIndices<1u,0u,0u,0u,false,false,0u,0u>)
|
|
|
|
INSTANCE(BlackOilIndices<0u,1u,0u,0u,false,false,0u,0u>)
|
|
|
|
INSTANCE(BlackOilIndices<0u,0u,1u,0u,false,false,0u,0u>)
|
|
|
|
INSTANCE(BlackOilIndices<0u,0u,0u,1u,false,false,0u,0u>)
|
|
|
|
INSTANCE(BlackOilIndices<0u,0u,0u,0u,false,false,1u,0u>)
|
|
|
|
INSTANCE(BlackOilIndices<0u,0u,0u,1u,false,true,0u,0u>)
|
2021-06-03 08:34:14 -05:00
|
|
|
|
|
|
|
} // namespace Opm
|