/* Copyright 2016 SINTEF ICT, Applied Mathematics. This file is part of the Open Porous Media project (OPM). OPM is free software: you can redistribute it and/or modify it under the terms of the GNU General Public License as published by the Free Software Foundation, either version 3 of the License, or (at your option) any later version. OPM is distributed in the hope that it will be useful, but WITHOUT ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License for more details. You should have received a copy of the GNU General Public License along with OPM. If not, see . */ #ifndef OPM_BLACKOILREORDERINGTRANSPORTMODEL_HEADER_INCLUDED #define OPM_BLACKOILREORDERINGTRANSPORTMODEL_HEADER_INCLUDED #include #include #include #include #include #include #include #include #include namespace Opm { namespace detail { template struct CreateVariable { Scalar operator()(double value, int index) { return Scalar::createVariable(value, index); } }; template <> struct CreateVariable { double operator()(double value, int) { return value; } }; template struct CreateConstant { Scalar operator()(double value) { return Scalar::createConstant(value); } }; template <> struct CreateConstant { double operator()(double value) { return value; } }; struct Connection { Connection(const int ind, const double s) : index(ind), sign(s) {} int index; double sign; }; class Connections; class ConnectivityGraph { public: explicit ConnectivityGraph(const HelperOps& ops) : grad_(ops.grad) , div_(ops.div) { grad_ia_ = grad_.outerIndexPtr(); grad_ja_ = grad_.innerIndexPtr(); grad_sign_ = grad_.valuePtr(); div_ia_ = div_.outerIndexPtr(); div_ja_ = div_.innerIndexPtr(); div_sign_ = div_.valuePtr(); } Connections cellConnections(const int cell) const; std::array connectionCells(const int connection) const { const int pos = div_ia_[connection]; assert(div_ia_[connection + 1] == pos + 2); const double sign1 = div_sign_[pos]; assert(div_sign_[pos + 1] == -sign1); if (sign1 > 0.0) { return {{ div_ja_[pos], div_ja_[pos + 1] }}; } else { return {{ div_ja_[pos + 1], div_ja_[pos] }}; } } private: friend class Connections; typedef HelperOps::M M; const M& grad_; const M& div_; const int* grad_ia_; const int* grad_ja_; const double* grad_sign_; const int* div_ia_; const int* div_ja_; const double* div_sign_; }; class Connections { public: Connections(const ConnectivityGraph& cg, const int cell) : cg_(cg), cell_(cell) {} int size() const { return cg_.grad_ia_[cell_ + 1] - cg_.grad_ia_[cell_]; } class Iterator { public: Iterator(const Connections& c, const int index) : c_(c), index_(index) {} Iterator& operator++() { ++index_; return *this; } bool operator!=(const Iterator& other) { assert(&c_ == &other.c_); return index_ != other.index_; } Connection operator*() { assert(index_ >= 0 && index_ < c_.size()); const int pos = c_.cg_.grad_ia_[c_.cell_] + index_; return Connection(c_.cg_.grad_ja_[pos], -c_.cg_.grad_sign_[pos]); // Note the minus sign! } private: const Connections& c_; int index_; }; Iterator begin() const { return Iterator(*this, 0); } Iterator end() const { return Iterator(*this, size()); } private: friend class Iterator; const ConnectivityGraph& cg_; const int cell_; }; inline Connections ConnectivityGraph::cellConnections(const int cell) const { return Connections(*this, cell); } } // namespace detail /// A model implementation for the transport equation in three-phase black oil. template class BlackoilReorderingTransportModel : public BlackoilModelBase > { public: typedef BlackoilModelBase > Base; friend Base; typedef typename Base::ReservoirState ReservoirState; typedef typename Base::WellState WellState; typedef typename Base::SolutionState SolutionState; typedef typename Base::V V; /// Construct the model. It will retain references to the /// arguments of this functions, and they are expected to /// remain in scope for the lifetime of the solver. /// \param[in] param parameters /// \param[in] grid grid data structure /// \param[in] fluid fluid properties /// \param[in] geo rock properties /// \param[in] rock_comp_props if non-null, rock compressibility properties /// \param[in] wells_arg well structure /// \param[in] linsolver linear solver /// \param[in] eclState eclipse state /// \param[in] has_disgas turn on dissolved gas /// \param[in] has_vapoil turn on vaporized oil feature /// \param[in] terminal_output request output to cout/cerr BlackoilReorderingTransportModel(const typename Base::ModelParameters& param, const Grid& grid, const BlackoilPropsAdFromDeck& fluid, const DerivedGeology& geo, const RockCompressibility* rock_comp_props, const StandardWells& std_wells, const NewtonIterationBlackoilInterface& linsolver, std::shared_ptr eclState, std::shared_ptr schedule, std::shared_ptr summary_config, const bool has_disgas, const bool has_vapoil, const bool terminal_output) : Base(param, grid, fluid, geo, rock_comp_props, std_wells, linsolver, eclState, schedule, summary_config, has_disgas, has_vapoil, terminal_output) , graph_(Base::ops_) , props_(dynamic_cast(fluid)) // TODO: remove the need for this cast. , state0_{ ReservoirState(0, 0, 0), WellState(), V(), V() } , state_{ ReservoirState(0, 0, 0), WellState(), V(), V() } , tr_model_(param, grid, fluid, geo, rock_comp_props, std_wells, linsolver, eclState, schedule, summary_config, has_disgas, has_vapoil, terminal_output) { // Set up the common parts of the mass balance equations // for each active phase. const V transi = subset(geo_.transmissibility(), ops_.internal_faces); const V trans_nnc = ops_.nnc_trans; trans_all_ = V::Zero(transi.size() + trans_nnc.size()); trans_all_ << transi, trans_nnc; gdz_ = geo_.gravity()[2] * (ops_.grad * geo_.z().matrix()); rhos_ = DataBlock::Zero(ops_.div.rows(), 3); rhos_.col(Water) = props_.surfaceDensity(Water, Base::cells_); rhos_.col(Oil) = props_.surfaceDensity(Oil, Base::cells_); rhos_.col(Gas) = props_.surfaceDensity(Gas, Base::cells_); } void prepareStep(const SimulatorTimerInterface& timer, const ReservoirState& reservoir_state, const WellState& well_state) { tr_model_.prepareStep(timer, reservoir_state, well_state); Base::prepareStep(timer, reservoir_state, well_state); Base::param_.solve_welleq_initially_ = false; state0_.reservoir_state = reservoir_state; state0_.well_state = well_state; // Since (reference) pressure is constant, porosity and transmissibility multipliers can // be computed just once. const std::vector& p = reservoir_state.pressure(); state0_.tr_mult = Base::transMult(ADB::constant(Eigen::Map(p.data(), p.size()))).value(); state0_.pv_mult = Base::poroMult(ADB::constant(Eigen::Map(p.data(), p.size()))).value(); const int num_cells = p.size(); cstate0_.resize(num_cells); for (int cell = 0; cell < num_cells; ++cell) { computeCellState(cell, state0_, cstate0_[cell]); } cstate_ = cstate0_; } template SimulatorReport nonlinearIteration(const int iteration, const SimulatorTimerInterface& timer, NonlinearSolverType& nonlinear_solver, ReservoirState& reservoir_state, const WellState& well_state) { // Extract reservoir and well fluxes and state. { DebugTimeReport tr("Extracting fluxes"); extractFluxes(reservoir_state, well_state); extractState(reservoir_state, well_state); } // Compute cell ordering based on total flux. { DebugTimeReport tr("Topological sort"); computeOrdering(); } // Solve in every component (cell or block of cells), in order. { DebugTimeReport tr("Solving all components"); for (int ii = 0; ii < 5; ++ii) { DebugTimeReport tr2("Solving components single sweep."); solveComponents(); } } // Update states for output. reservoir_state = state_.reservoir_state; // Assemble with other model, { auto rs = reservoir_state; auto ws = well_state; tr_model_.nonlinearIteration(/*iteration*/ 0, timer, nonlinear_solver, rs, ws); } // Create report and exit. SimulatorReport report; report.converged = true; return report; } void afterStep(const SimulatorTimerInterface& /* timer */, const ReservoirState& /* reservoir_state */, const WellState& /* well_state */) { // Does nothing in this model. } using Base::numPhases; protected: // ============ Types ============ using Vec2 = Dune::FieldVector; using Mat22 = Dune::FieldMatrix; using Eval = DenseAd::Evaluation; struct State { ReservoirState reservoir_state; WellState well_state; V tr_mult; V pv_mult; }; template struct CellState { using Scalar = ScalarT; Scalar s[3]; Scalar rs; Scalar rv; Scalar p[3]; Scalar kr[3]; Scalar pc[3]; Scalar temperature; Scalar mu[3]; Scalar b[3]; Scalar lambda[3]; Scalar rho[3]; Scalar rssat; Scalar rvsat; // Implement interface used for opm-material properties. const Scalar& saturation(int phaseIdx) const { return s[phaseIdx]; } template CellState flatten() const { return CellState{ { s[0].value(), s[1].value(), s[2].value() }, rs.value(), rv.value(), { p[0].value(), p[1].value(), p[2].value() }, { kr[0].value(), kr[1].value(), kr[2].value() }, { pc[0].value(), pc[1].value(), pc[2].value() }, temperature.value(), { mu[0].value(), mu[1].value(), mu[2].value() }, { b[0].value(), b[1].value(), b[2].value() }, { lambda[0].value(), lambda[1].value(), lambda[2].value() }, { rho[0].value(), rho[1].value(), rho[2].value() }, rssat.value(), rvsat.value() }; } }; // ============ Data members ============ using Base::grid_; using Base::geo_; using Base::ops_; const detail::ConnectivityGraph graph_; const BlackoilPropsAdFromDeck& props_; State state0_; State state_; std::vector> cstate0_; std::vector> cstate_; V total_flux_; V total_wellperf_flux_; DataBlock comp_wellperf_flux_; V total_wellflux_cell_; V oil_wellflux_cell_; V gas_wellflux_cell_; std::vector sequence_; std::vector components_; V trans_all_; V gdz_; DataBlock rhos_; std::array max_abs_dx_; std::array max_abs_dx_cell_; // TODO: remove this, for debug only. BlackoilTransportModel tr_model_; // ============ Member functions ============ template void computeCellState(const int cell, const State& state, CellState& cstate) const { assert(numPhases() == 3); // I apologize for this to my future self, that will have to fix it. // Extract from state and props. const auto hcstate = state.reservoir_state.hydroCarbonState()[cell]; const bool is_sg = (hcstate == HydroCarbonState::GasAndOil); const bool is_rs = (hcstate == HydroCarbonState::OilOnly); const bool is_rv = (hcstate == HydroCarbonState::GasOnly); const double swval = state.reservoir_state.saturation()[3*cell + Water]; const double sgval = state.reservoir_state.saturation()[3*cell + Gas]; const double rsval = state.reservoir_state.gasoilratio()[cell]; const double rvval = state.reservoir_state.rv()[cell]; const double poval = state.reservoir_state.pressure()[cell]; const int pvt_region = props_.pvtRegions()[cell]; // Property functions. const auto& waterpvt = props_.waterProps(); const auto& oilpvt = props_.oilProps(); const auto& gaspvt = props_.gasProps(); const auto& satfunc = props_.materialLaws(); // Create saturation and composition variables. detail::CreateVariable variable; detail::CreateConstant constant; cstate.s[Water] = variable(swval, 0); cstate.s[Gas] = is_sg ? variable(sgval, 1) : constant(sgval); cstate.s[Oil] = 1.0 - cstate.s[Water] - cstate.s[Gas]; cstate.rs = is_rs ? variable(rsval, 1) : constant(rsval); cstate.rv = is_rv ? variable(rvval, 1) : constant(rvval); // Compute relative permeabilities amd capillary pressures. const auto& params = satfunc.materialLawParams(cell); typedef BlackoilPropsAdFromDeck::MaterialLawManager::MaterialLaw MaterialLaw; MaterialLaw::relativePermeabilities(cstate.kr, params, cstate); MaterialLaw::capillaryPressures(cstate.pc, params, cstate); // Compute phase pressures. cstate.p[Oil] = constant(poval); cstate.p[Water] = cstate.p[Oil] + cstate.pc[Water]; // pcow = pw - po (!) [different from old convention] cstate.p[Gas] = cstate.p[Oil] + cstate.pc[Gas]; // pcog = pg - po // Compute PVT properties. cstate.temperature = constant(0.0); // Temperature is not used. cstate.mu[Water] = waterpvt.viscosity(pvt_region, cstate.temperature, cstate.p[Water]); cstate.mu[Oil] = is_sg ? oilpvt.saturatedViscosity(pvt_region, cstate.temperature, cstate.p[Oil]) : oilpvt.viscosity(pvt_region, cstate.temperature, cstate.p[Oil], cstate.rs); cstate.mu[Gas] = is_sg ? gaspvt.saturatedViscosity(pvt_region, cstate.temperature, cstate.p[Gas]) : gaspvt.viscosity(pvt_region, cstate.temperature, cstate.p[Gas], cstate.rv); cstate.b[Water] = waterpvt.inverseFormationVolumeFactor(pvt_region, cstate.temperature, cstate.p[Water]); cstate.b[Oil] = is_sg ? oilpvt.saturatedInverseFormationVolumeFactor(pvt_region, cstate.temperature, cstate.p[Oil]) : oilpvt.inverseFormationVolumeFactor(pvt_region, cstate.temperature, cstate.p[Oil], cstate.rs); cstate.b[Gas] = is_sg ? gaspvt.saturatedInverseFormationVolumeFactor(pvt_region, cstate.temperature, cstate.p[Gas]) : gaspvt.inverseFormationVolumeFactor(pvt_region, cstate.temperature, cstate.p[Gas], cstate.rv); // Compute mobilities. for (int phase = 0; phase < 3; ++phase) { cstate.lambda[phase] = cstate.kr[phase] / cstate.mu[phase]; } // Compute densities. cstate.rho[Water] = rhos_(cell, Water) * cstate.b[Water]; cstate.rho[Oil] = (rhos_(cell, Oil) + cstate.rs*rhos_(cell, Gas)) * cstate.b[Oil]; // TODO: check that this is correct cstate.rho[Gas] = (rhos_(cell, Gas) + cstate.rv*rhos_(cell, Oil)) * cstate.b[Gas]; // Compute saturated rs and rv factors. cstate.rssat = oilpvt.saturatedGasDissolutionFactor(pvt_region, cstate.temperature, cstate.p[Oil]); cstate.rvsat = gaspvt.saturatedOilVaporizationFactor(pvt_region, cstate.temperature, cstate.p[Gas]); // TODO: add vaporization controls such as in BlackoilPropsAdFromDeck::applyVap(). } void extractFluxes(const ReservoirState& reservoir_state, const WellState& well_state) { // Input face fluxes are for interior faces + nncs. total_flux_ = Eigen::Map(reservoir_state.faceflux().data(), reservoir_state.faceflux().size()); total_wellperf_flux_ = Eigen::Map(well_state.perfRates().data(), well_state.perfRates().size()); comp_wellperf_flux_ = Eigen::Map(well_state.perfPhaseRates().data(), well_state.perfRates().size(), numPhases()); const int num_cells = reservoir_state.pressure().size(); total_wellflux_cell_ = superset(total_wellperf_flux_, Base::wellModel().wellOps().well_cells, num_cells); assert(Base::numPhases() == 3); V oilflux = comp_wellperf_flux_.col(1); V gasflux = comp_wellperf_flux_.col(2); oil_wellflux_cell_ = superset(oilflux, Base::wellModel().wellOps().well_cells, num_cells); gas_wellflux_cell_ = superset(gasflux, Base::wellModel().wellOps().well_cells, num_cells); assert(numPhases() * well_state.perfRates().size() == well_state.perfPhaseRates().size()); } void extractState(const ReservoirState& reservoir_state, const WellState& well_state) { state_.reservoir_state = reservoir_state; state_.well_state = well_state; const std::vector& p = reservoir_state.pressure(); state_.tr_mult = Base::transMult(ADB::constant(Eigen::Map(p.data(), p.size()))).value(); state_.pv_mult = Base::poroMult(ADB::constant(Eigen::Map(p.data(), p.size()))).value(); } void computeOrdering() { assert(!geo_.nnc().hasNNC()); // TODO: support compute_sequence() with grid + nnc. static_assert(std::is_same::value, "compute_sequence() is written in C and therefore requires an UnstructuredGrid, " "it must be rewritten to use other grid classes such as CpGrid"); using namespace Opm::AutoDiffGrid; const int num_cells = numCells(grid_); sequence_.resize(num_cells); components_.resize(num_cells + 1); // max possible size int num_components = -1; using namespace Opm::AutoDiffGrid; const int num_faces = numFaces(grid_); V flux_on_all_faces = superset(total_flux_, ops_.internal_faces, num_faces); compute_sequence(&grid_, flux_on_all_faces.data(), sequence_.data(), components_.data(), &num_components); OpmLog::debug(std::string("Number of components: ") + std::to_string(num_components)); components_.resize(num_components + 1); // resize to fit actually used part } void solveComponents() { // Zero the max changed. max_abs_dx_[0] = 0.0; max_abs_dx_[1] = 0.0; max_abs_dx_cell_[0] = -1; max_abs_dx_cell_[1] = -1; // Solve the equations. const int num_components = components_.size() - 1; for (int comp = 0; comp < num_components; ++comp) { const int comp_size = components_[comp + 1] - components_[comp]; if (comp_size == 1) { solveSingleCell(sequence_[components_[comp]]); } else { solveMultiCell(comp_size, &sequence_[components_[comp]]); } } // Log the max change. { std::ostringstream os; os << "=== Max abs dx[0]: " << max_abs_dx_[0] << " (cell " << max_abs_dx_cell_[0] <<") dx[1]: " << max_abs_dx_[1] << " (cell " << max_abs_dx_cell_[1] << ")"; OpmLog::debug(os.str()); } } void solveSingleCell(const int cell) { Vec2 res; Mat22 jac; assembleSingleCell(cell, res, jac); // Newton loop. int iter = 0; const int max_iter = 100; double relaxation = 1.0; while (!getConvergence(cell, res) && iter < max_iter) { Vec2 dx; jac.solve(dx, res); dx *= relaxation; // const auto hcstate_old = state_.reservoir_state.hydroCarbonState()[cell]; updateState(cell, -dx); // const auto hcstate = state_.reservoir_state.hydroCarbonState()[cell]; assembleSingleCell(cell, res, jac); ++iter; if (iter > 10) { relaxation = 0.85; if (iter > 15) { relaxation = 0.70; } if (iter > 20) { relaxation = 0.55; } if (iter > 25) { relaxation = 0.40; } if (iter > 30) { relaxation = 0.25; } // std::ostringstream os; // os << "Iteration " << iter << " in cell " << cell << ", residual = " << res // << ", cell values { s = ( " << cstate_[cell].s[Water] << ", " << cstate_[cell].s[Oil] << ", " << cstate_[cell].s[Gas] // << " ), rs = " << cstate_[cell].rs << ", rv = " << cstate_[cell].rv << "}, dx = " << dx << ", hcstate: " << hcstate_old << " -> " << hcstate; // OpmLog::debug(os.str()); } } if (iter == max_iter) { std::ostringstream os; os << "Failed to converge in cell " << cell << ", residual = " << res << ", cell values { s = ( " << cstate_[cell].s[Water] << ", " << cstate_[cell].s[Oil] << ", " << cstate_[cell].s[Gas] << " ), rs = " << cstate_[cell].rs << ", rv = " << cstate_[cell].rv << " }"; OpmLog::debug(os.str()); } } void solveMultiCell(const int comp_size, const int* cell_array) { // OpmLog::warning("solveMultiCell", "solveMultiCell() called with component size " + std::to_string(comp_size)); for (int ii = 0; ii < comp_size; ++ii) { solveSingleCell(cell_array[ii]); } } template Scalar oilAccumulation(const CellState& cs) { return cs.b[Oil]*cs.s[Oil] + cs.rv*cs.b[Gas]*cs.s[Gas]; } template Scalar gasAccumulation(const CellState& cs) { return cs.b[Gas]*cs.s[Gas] + cs.rs*cs.b[Oil]*cs.s[Oil]; } void applyThresholdPressure(const int connection, Eval& dp) { const double thres_press = Base::threshold_pressures_by_connection_[connection]; if (std::fabs(dp.value()) < thres_press) { dp.setValue(0.0); } else { dp -= dp.value() > 0.0 ? thres_press : -thres_press; } } void assembleSingleCell(const int cell, Vec2& res, Mat22& jac) { assert(numPhases() == 3); // I apologize for this to my future self, that will have to fix it. CellState st; computeCellState(cell, state_, st); cstate_[cell] = st.template flatten(); // Accumulation terms. const double pvm0 = state0_.pv_mult[cell]; const double pvm = state_.pv_mult[cell]; const double ao0 = oilAccumulation(cstate0_[cell]) * pvm0; const Eval ao = oilAccumulation(st) * pvm; const double ag0 = gasAccumulation(cstate0_[cell]) * pvm0; const Eval ag = gasAccumulation(st) * pvm; // Flux terms. Eval div_oilflux = Eval::createConstant(0.0); Eval div_gasflux = Eval::createConstant(0.0); for (auto conn : graph_.cellConnections(cell)) { auto conn_cells = graph_.connectionCells(conn.index); const int from = conn_cells[0]; const int to = conn_cells[1]; if (from < 0 || to < 0) { continue; // Boundary. } assert((from == cell) == (conn.sign > 0.0)); const int other = from == cell ? to : from; const double vt = conn.sign * total_flux_[conn.index]; const double gdz = conn.sign * gdz_[conn.index]; // From this point, we treat everything about this // connection as going from 'cell' to 'other'. Since // we don't want derivatives from the 'other' cell to // participate in the solution, we use the constant // values from cstate_[other]. Eval dh[3]; Eval dh_sat[3]; const Eval grad_oil_press = cstate_[other].p[Oil] - st.p[Oil]; for (int phase : { Water, Oil, Gas }) { const Eval gradp = cstate_[other].p[phase] - st.p[phase]; const Eval rhoavg = 0.5 * (st.rho[phase] + cstate_[other].rho[phase]); dh[phase] = gradp - rhoavg * gdz; if (Base::use_threshold_pressure_) { applyThresholdPressure(conn.index, dh[phase]); } dh_sat[phase] = grad_oil_press - dh[phase]; } const double tran = trans_all_[conn.index]; // TODO: include tr_mult effect. const auto& m1 = st.lambda; const auto& m2 = cstate_[other].lambda; const auto upw = connectionMultiPhaseUpwind({{ dh_sat[Water].value(), dh_sat[Oil].value(), dh_sat[Gas].value() }}, {{ m1[Water].value(), m1[Oil].value(), m1[Gas].value() }}, {{ m2[Water], m2[Oil], m2[Gas] }}, tran, vt); // if (upw[0] != upw[1] || upw[1] != upw[2]) { // OpmLog::debug("Detected countercurrent flow between cells " + std::to_string(from) + " and " + std::to_string(to)); // } Eval b[3]; Eval mob[3]; Eval tot_mob = Eval::createConstant(0.0); for (int phase : { Water, Oil, Gas }) { b[phase] = upw[phase] > 0.0 ? st.b[phase] : cstate_[other].b[phase]; mob[phase] = upw[phase] > 0.0 ? m1[phase] : m2[phase]; tot_mob += mob[phase]; } Eval rs = upw[Oil] > 0.0 ? st.rs : cstate_[other].rs; Eval rv = upw[Gas] > 0.0 ? st.rv : cstate_[other].rv; Eval flux[3]; for (int phase : { Oil, Gas }) { Eval gflux = Eval::createConstant(0.0); for (int other_phase : { Water, Oil, Gas }) { if (phase != other_phase) { gflux += mob[other_phase] * (dh_sat[phase] - dh_sat[other_phase]); } } flux[phase] = b[phase] * (mob[phase] / tot_mob) * (vt + tran*gflux); } div_oilflux += flux[Oil] + rv*flux[Gas]; div_gasflux += flux[Gas] + rs*flux[Oil]; } // Well fluxes. if (total_wellflux_cell_[cell] > 0.0) { // Injecting perforation. Use given phase rates. assert(oil_wellflux_cell_[cell] >= 0.0); assert(gas_wellflux_cell_[cell] >= 0.0); div_oilflux -= oil_wellflux_cell_[cell]; div_gasflux -= gas_wellflux_cell_[cell]; } else if (total_wellflux_cell_[cell] < 0.0) { // Producing perforation. Use total rate and fractional flow. Eval totmob = st.lambda[Water] + st.lambda[Oil] + st.lambda[Gas]; Eval oilflux = st.b[Oil] * (st.lambda[Oil]/totmob) * total_wellflux_cell_[cell]; Eval gasflux = st.b[Gas] * (st.lambda[Gas]/totmob) * total_wellflux_cell_[cell]; div_oilflux -= (oilflux + st.rv * gasflux); div_gasflux -= (gasflux + st.rs * oilflux); } const Eval oileq = Base::pvdt_[cell]*(ao - ao0) + div_oilflux; const Eval gaseq = Base::pvdt_[cell]*(ag - ag0) + div_gasflux; res[0] = oileq.value(); res[1] = gaseq.value(); jac[0][0] = oileq.derivative(0); jac[0][1] = oileq.derivative(1); jac[1][0] = gaseq.derivative(0); jac[1][1] = gaseq.derivative(1); } bool getConvergence(const int cell, const Vec2& res) { const double tol = 1e-7; // Compute scaled residuals (scaled like saturations). double sres[] = { res[0] / (cstate_[cell].b[Oil] * Base::pvdt_[cell]), res[1] / (cstate_[cell].b[Gas] * Base::pvdt_[cell]) }; return std::fabs(sres[0]) < tol && std::fabs(sres[1]) < tol; } void updateState(const int cell, const Vec2& dx) { if (std::fabs(dx[0]) > max_abs_dx_[0]) { max_abs_dx_cell_[0] = cell; } if (std::fabs(dx[1]) > max_abs_dx_[1]) { max_abs_dx_cell_[1] = cell; } max_abs_dx_[0] = std::max(max_abs_dx_[0], std::fabs(dx[0])); max_abs_dx_[1] = std::max(max_abs_dx_[1], std::fabs(dx[1])); // Get saturation updates. const double dsw = dx[0]; double dsg = 0.0; auto& hcstate = state_.reservoir_state.hydroCarbonState()[cell]; if (hcstate == HydroCarbonState::GasAndOil) { dsg = dx[1]; } else if (hcstate == HydroCarbonState::GasOnly) { dsg = -dsw; } const double dso = -(dsw + dsg); // Handle too large saturation changes. const double maxval = std::max(std::fabs(dsw), std::max(std::fabs(dso), std::fabs(dsg))); const double sfactor = std::min(1.0, Base::dsMax() / maxval); double* s = state_.reservoir_state.saturation().data() + 3*cell; s[Water] += sfactor*dsw; s[Gas] += sfactor*dsg; s[Oil] = 1.0 - s[Water] - s[Gas]; // Handle < 0 saturations. for (int phase : { Gas, Oil, Water }) { // TODO: check if ordering here is significant if (s[phase] < 0.0) { for (int other_phase : { Water, Oil, Gas }) { if (phase != other_phase) { s[other_phase] /= (1.0 - s[phase]); } } s[phase] = 0.0; } } // Update rs. double& rs = state_.reservoir_state.gasoilratio()[cell]; const double rs_old = rs; if (hcstate == HydroCarbonState::OilOnly) { // const double max_allowed_change = std::fabs(rs_old) * Base::drMaxRel(); const double drs = dx[1]; // const double factor = std::min(1.0, max_allowed_change / std::fabs(drs)); // rs += factor*drs; rs += drs; rs = std::max(rs, 0.0); } // Update rv. double& rv = state_.reservoir_state.rv()[cell]; const double rv_old = rv; if (hcstate == HydroCarbonState::GasOnly) { // const double max_allowed_change = std::fabs(rv_old) * Base::drMaxRel(); const double drv = dx[1]; // const double factor = std::min(1.0, max_allowed_change / std::fabs(drv)); // rv += factor*drv; rv += drv; rv = std::max(rv, 0.0); } const double epsilon = std::sqrt(std::numeric_limits::epsilon()); const bool water_only = s[Water] > (1 - epsilon); const auto old_hcstate = hcstate; hcstate = HydroCarbonState::GasAndOil; // sg <-> rs transition. { const double rssat_old = cstate_[cell].rssat; const double rssat = rssat_old; // TODO: This is no longer true with vaporization controls const bool is_rs = old_hcstate == HydroCarbonState::OilOnly; const bool has_gas = (s[Gas] > 0.0 && !is_rs); const bool gas_vaporized = ( (rs > rssat * (1+epsilon) && is_rs ) && (rs_old > rssat_old * (1-epsilon)) ); if (water_only || has_gas || gas_vaporized) { rs = rssat; } else { hcstate = HydroCarbonState::OilOnly; } } // sg <-> rv transition. { const double rvsat_old = cstate_[cell].rvsat; const double rvsat = rvsat_old; // TODO: This is no longer true with vaporization controls const bool is_rv = old_hcstate == HydroCarbonState::GasOnly; const bool has_oil = (s[Oil] > 0.0 && !is_rv); const bool oil_condensed = ( (rv > rvsat * (1+epsilon) && is_rv) && (rv_old > rvsat_old * (1-epsilon)) ); if (water_only || has_oil || oil_condensed) { rv = rvsat; } else { hcstate = HydroCarbonState::GasOnly; } } } }; /// Providing types by template specialisation of ModelTraits for BlackoilReorderingTransportModel. template struct ModelTraits< BlackoilReorderingTransportModel > { typedef BlackoilState ReservoirState; typedef WellStateFullyImplicitBlackoil WellState; typedef BlackoilModelParameters ModelParameters; typedef DefaultBlackoilSolutionState SolutionState; }; } // namespace Opm #endif // OPM_BLACKOILREORDERINGTRANSPORTMODEL_HEADER_INCLUDED