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| 1 | // -*- mode: C++; tab-width: 4; indent-tabs-mode: nil; c-basic-offset: 4 -*- | ||
| 2 | // vi: set et ts=4 sw=4 sts=4: | ||
| 3 | // | ||
| 4 | // SPDX-FileCopyrightInfo: Copyright © DuMux Project contributors, see AUTHORS.md in root folder | ||
| 5 | // SPDX-License-Identifier: GPL-3.0-or-later | ||
| 6 | // | ||
| 7 | /*! | ||
| 8 | * \file | ||
| 9 | * \ingroup BoundaryTests | ||
| 10 | * \brief A simple Stokes test problem for the staggered grid (Navier-)Stokes model. | ||
| 11 | */ | ||
| 12 | |||
| 13 | #ifndef DUMUX_STOKES1P2C_SUBPROBLEM_HH | ||
| 14 | #define DUMUX_STOKES1P2C_SUBPROBLEM_HH | ||
| 15 | |||
| 16 | #include <dumux/common/properties.hh> | ||
| 17 | #include <dumux/common/parameters.hh> | ||
| 18 | #include <dumux/common/timeloop.hh> | ||
| 19 | #include <dumux/common/numeqvector.hh> | ||
| 20 | |||
| 21 | #include <dumux/freeflow/navierstokes/boundarytypes.hh> | ||
| 22 | #include <dumux/freeflow/navierstokes/staggered/problem.hh> | ||
| 23 | |||
| 24 | #include <dumux/multidomain/boundary/stokesdarcy/couplingdata.hh> | ||
| 25 | |||
| 26 | namespace Dumux { | ||
| 27 | |||
| 28 | /*! | ||
| 29 | * \ingroup BoundaryTests | ||
| 30 | * \brief Test problem for the one-phase (Navier-) Stokes problem. | ||
| 31 | * | ||
| 32 | * Horizontal flow from left to right with a parabolic velocity profile. | ||
| 33 | */ | ||
| 34 | template <class TypeTag> | ||
| 35 | class StokesSubProblem : public NavierStokesStaggeredProblem<TypeTag> | ||
| 36 | { | ||
| 37 | using ParentType = NavierStokesStaggeredProblem<TypeTag>; | ||
| 38 | |||
| 39 | using GridView = typename GetPropType<TypeTag, Properties::GridGeometry>::GridView; | ||
| 40 | using Scalar = GetPropType<TypeTag, Properties::Scalar>; | ||
| 41 | using FluidSystem = GetPropType<TypeTag, Properties::FluidSystem>; | ||
| 42 | using Indices = typename GetPropType<TypeTag, Properties::ModelTraits>::Indices; | ||
| 43 | using BoundaryTypes = Dumux::NavierStokesBoundaryTypes<GetPropType<TypeTag, Properties::ModelTraits>::numEq()>; | ||
| 44 | |||
| 45 | using GridGeometry = GetPropType<TypeTag, Properties::GridGeometry>; | ||
| 46 | using FVElementGeometry = typename GridGeometry::LocalView; | ||
| 47 | using SubControlVolumeFace = typename FVElementGeometry::SubControlVolumeFace; | ||
| 48 | using Element = typename GridView::template Codim<0>::Entity; | ||
| 49 | using ElementVolumeVariables = typename GetPropType<TypeTag, Properties::GridVolumeVariables>::LocalView; | ||
| 50 | using ElementFaceVariables = typename GetPropType<TypeTag, Properties::GridFaceVariables>::LocalView; | ||
| 51 | using FluidState = GetPropType<TypeTag, Properties::FluidState>; | ||
| 52 | |||
| 53 | using GlobalPosition = typename Element::Geometry::GlobalCoordinate; | ||
| 54 | |||
| 55 | using PrimaryVariables = GetPropType<TypeTag, Properties::PrimaryVariables>; | ||
| 56 | using NumEqVector = Dumux::NumEqVector<PrimaryVariables>; | ||
| 57 | |||
| 58 | using CouplingManager = GetPropType<TypeTag, Properties::CouplingManager>; | ||
| 59 | using TimeLoopPtr = std::shared_ptr<TimeLoop<Scalar>>; | ||
| 60 | |||
| 61 | using DiffusionCoefficientAveragingType = typename StokesDarcyCouplingOptions::DiffusionCoefficientAveragingType; | ||
| 62 | |||
| 63 | static constexpr bool useMoles = GetPropType<TypeTag, Properties::ModelTraits>::useMoles(); | ||
| 64 | |||
| 65 | public: | ||
| 66 | 2 | StokesSubProblem(std::shared_ptr<const GridGeometry> gridGeometry, std::shared_ptr<CouplingManager> couplingManager) | |
| 67 |
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6 | : ParentType(gridGeometry, "Stokes"), eps_(1e-6), couplingManager_(couplingManager) |
| 68 | { | ||
| 69 |
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4 | refVelocity_ = getParamFromGroup<Scalar>(this->paramGroup(), "Problem.RefVelocity"); |
| 70 |
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2 | refPressure_ = getParamFromGroup<Scalar>(this->paramGroup(), "Problem.RefPressure"); |
| 71 |
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2 | refMoleFrac_ = getParamFromGroup<Scalar>(this->paramGroup(), "Problem.refMoleFrac"); |
| 72 |
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2 | refTemperature_ = getParamFromGroup<Scalar>(this->paramGroup(), "Problem.RefTemperature"); |
| 73 | |||
| 74 |
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2 | diffCoeffAvgType_ = StokesDarcyCouplingOptions::stringToEnum(DiffusionCoefficientAveragingType{}, |
| 75 |
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2 | getParamFromGroup<std::string>(this->paramGroup(), "Problem.InterfaceDiffusionCoefficientAvg")); |
| 76 |
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2 | problemName_ = getParam<std::string>("Vtk.OutputName") + "_" + getParamFromGroup<std::string>(this->paramGroup(), "Problem.Name"); |
| 77 | 2 | } | |
| 78 | |||
| 79 | /*! | ||
| 80 | * \name Problem parameters | ||
| 81 | */ | ||
| 82 | // \{ | ||
| 83 | |||
| 84 | /*! | ||
| 85 | * \brief The problem name. | ||
| 86 | */ | ||
| 87 | const std::string& name() const | ||
| 88 | { | ||
| 89 |
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2 | return problemName_; |
| 90 | } | ||
| 91 | |||
| 92 | /*! | ||
| 93 | * \brief Returns the sources within the domain. | ||
| 94 | * | ||
| 95 | * \param globalPos The global position | ||
| 96 | */ | ||
| 97 | ✗ | NumEqVector sourceAtPos(const GlobalPosition &globalPos) const | |
| 98 | 3102464 | { return NumEqVector(0.0); } | |
| 99 | |||
| 100 | // \} | ||
| 101 | /*! | ||
| 102 | * \name Boundary conditions | ||
| 103 | */ | ||
| 104 | // \{ | ||
| 105 | |||
| 106 | /*! | ||
| 107 | * \brief Specifies which kind of boundary condition should be | ||
| 108 | * used for which equation on a given boundary segment. | ||
| 109 | * | ||
| 110 | * \param element The finite element | ||
| 111 | * \param scvf The sub control volume face | ||
| 112 | */ | ||
| 113 | 1649876 | BoundaryTypes boundaryTypes(const Element& element, | |
| 114 | const SubControlVolumeFace& scvf) const | ||
| 115 | { | ||
| 116 | 1649876 | BoundaryTypes values; | |
| 117 | |||
| 118 |
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1649876 | const auto& globalPos = scvf.center(); |
| 119 | |||
| 120 | #if NONISOTHERMAL | ||
| 121 |
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1034768 | values.setNeumann(Indices::energyEqIdx); |
| 122 | #endif | ||
| 123 | |||
| 124 | 6115576 | if (onUpperBoundary_(globalPos) || onLeftBoundary_(globalPos)) | |
| 125 | { | ||
| 126 | 747854 | values.setDirichlet(Indices::velocityXIdx); | |
| 127 | 747854 | values.setDirichlet(Indices::velocityYIdx); | |
| 128 | 747854 | values.setNeumann(Indices::conti0EqIdx); | |
| 129 | 747854 | values.setNeumann(Indices::conti0EqIdx + 1); | |
| 130 | } | ||
| 131 | |||
| 132 | 3299752 | if (onRightBoundary_(globalPos)) | |
| 133 | { | ||
| 134 | 574382 | values.setDirichlet(Indices::pressureIdx); | |
| 135 | 574382 | values.setOutflow(Indices::conti0EqIdx + 1); | |
| 136 | |||
| 137 | #if NONISOTHERMAL | ||
| 138 | 357480 | values.setOutflow(Indices::energyEqIdx); | |
| 139 | #endif | ||
| 140 | } | ||
| 141 | |||
| 142 |
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1649876 | if (couplingManager().isCoupledEntity(CouplingManager::stokesIdx, scvf)) |
| 143 | { | ||
| 144 | 327640 | values.setCouplingNeumann(Indices::conti0EqIdx); | |
| 145 | 327640 | values.setCouplingNeumann(Indices::conti0EqIdx + 1); | |
| 146 | 327640 | values.setCouplingNeumann(Indices::momentumYBalanceIdx); | |
| 147 | 327640 | values.setBeaversJoseph(Indices::momentumXBalanceIdx); | |
| 148 | } | ||
| 149 | 1649876 | return values; | |
| 150 | } | ||
| 151 | |||
| 152 | /*! | ||
| 153 | * \brief Evaluates the boundary conditions for a Dirichlet control volume. | ||
| 154 | */ | ||
| 155 | PrimaryVariables dirichletAtPos(const GlobalPosition& pos) const | ||
| 156 | { | ||
| 157 | 369988 | PrimaryVariables values(0.0); | |
| 158 |
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369988 | values = initialAtPos(pos); |
| 159 | |||
| 160 | return values; | ||
| 161 | } | ||
| 162 | |||
| 163 | /*! | ||
| 164 | * \brief Evaluates the boundary conditions for a Neumann control volume. | ||
| 165 | * | ||
| 166 | * \param element The element for which the Neumann boundary condition is set | ||
| 167 | * \param fvGeometry The fvGeometry | ||
| 168 | * \param elemVolVars The element volume variables | ||
| 169 | * \param elemFaceVars The element face variables | ||
| 170 | * \param scvf The boundary sub control volume face | ||
| 171 | */ | ||
| 172 | 194170 | NumEqVector neumann(const Element& element, | |
| 173 | const FVElementGeometry& fvGeometry, | ||
| 174 | const ElementVolumeVariables& elemVolVars, | ||
| 175 | const ElementFaceVariables& elemFaceVars, | ||
| 176 | const SubControlVolumeFace& scvf) const | ||
| 177 | { | ||
| 178 | 194170 | PrimaryVariables values(0.0); | |
| 179 | 194170 | const auto& globalPos = scvf.dofPosition(); | |
| 180 | 388340 | const auto& scv = fvGeometry.scv(scvf.insideScvIdx()); | |
| 181 | |||
| 182 | 194170 | FluidState fluidState; | |
| 183 | 194170 | updateFluidStateForBC_(fluidState, elemVolVars[scv].pressure()); | |
| 184 | |||
| 185 |
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194170 | const Scalar density = useMoles ? fluidState.molarDensity(0) : fluidState.density(0); |
| 186 | 388340 | const Scalar xVelocity = xVelocity_(globalPos); | |
| 187 | |||
| 188 | 388340 | if (onLeftBoundary_(globalPos)) | |
| 189 | { | ||
| 190 | // rho*v*X at inflow | ||
| 191 | 73894 | values[Indices::conti0EqIdx + 1] = -xVelocity * density * refMoleFrac(); | |
| 192 | 105568 | values[Indices::conti0EqIdx] = -xVelocity * density * (1.0 - refMoleFrac()); | |
| 193 | |||
| 194 | #if NONISOTHERMAL | ||
| 195 | 168880 | values[Indices::energyEqIdx] = -xVelocity * fluidState.density(0) * fluidState.enthalpy(0); | |
| 196 | #endif | ||
| 197 | } | ||
| 198 | |||
| 199 |
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194170 | if(couplingManager().isCoupledEntity(CouplingManager::stokesIdx, scvf)) |
| 200 | { | ||
| 201 | 85256 | values[Indices::momentumYBalanceIdx] = couplingManager().couplingData().momentumCouplingCondition(element, fvGeometry, elemVolVars, elemFaceVars, scvf); | |
| 202 | |||
| 203 | 85256 | const auto massFlux = couplingManager().couplingData().massCouplingCondition(element, fvGeometry, elemVolVars, elemFaceVars, scvf, diffCoeffAvgType_); | |
| 204 | 170512 | values[Indices::conti0EqIdx] = massFlux[0]; | |
| 205 | 207412 | values[Indices::conti0EqIdx + 1] = massFlux[1]; | |
| 206 | |||
| 207 | #if NONISOTHERMAL | ||
| 208 | 48356 | values[Indices::energyEqIdx] = couplingManager().couplingData().energyCouplingCondition(element, fvGeometry, elemVolVars, elemFaceVars, scvf, diffCoeffAvgType_); | |
| 209 | #endif | ||
| 210 | |||
| 211 | } | ||
| 212 | 194170 | return values; | |
| 213 | } | ||
| 214 | |||
| 215 | // \} | ||
| 216 | |||
| 217 | //! Get the coupling manager | ||
| 218 | const CouplingManager& couplingManager() const | ||
| 219 | 3858604 | { return *couplingManager_; } | |
| 220 | |||
| 221 | /*! | ||
| 222 | * \name Volume terms | ||
| 223 | */ | ||
| 224 | // \{ | ||
| 225 | |||
| 226 | /*! | ||
| 227 | * \brief Evaluates the initial value for a control volume. | ||
| 228 | * | ||
| 229 | * \param globalPos The global position | ||
| 230 | */ | ||
| 231 | 2871616 | PrimaryVariables initialAtPos(const GlobalPosition &globalPos) const | |
| 232 | { | ||
| 233 | 2871616 | FluidState fluidState; | |
| 234 | 2871616 | updateFluidStateForBC_(fluidState, refPressure()); | |
| 235 | |||
| 236 | 2871616 | const Scalar density = FluidSystem::density(fluidState, 0); | |
| 237 | |||
| 238 | 2871616 | PrimaryVariables values(0.0); | |
| 239 | 22972928 | values[Indices::pressureIdx] = refPressure() + density*this->gravity()[1]*(globalPos[1] - this->gridGeometry().bBoxMin()[1]); | |
| 240 | 5743232 | values[Indices::conti0EqIdx + 1] = refMoleFrac(); | |
| 241 | 8614848 | values[Indices::velocityXIdx] = xVelocity_(globalPos); | |
| 242 | |||
| 243 | #if NONISOTHERMAL | ||
| 244 | 3168344 | values[Indices::temperatureIdx] = refTemperature(); | |
| 245 | #endif | ||
| 246 | |||
| 247 | 2871616 | return values; | |
| 248 | } | ||
| 249 | |||
| 250 | //! Returns the reference velocity. | ||
| 251 | ✗ | const Scalar refVelocity() const | |
| 252 | ✗ | { return refVelocity_ ;} | |
| 253 | |||
| 254 | //! Returns the reference pressure. | ||
| 255 | ✗ | const Scalar refPressure() const | |
| 256 | ✗ | { return refPressure_; } | |
| 257 | |||
| 258 | //! Returns the reference mass fraction. | ||
| 259 | ✗ | const Scalar refMoleFrac() const | |
| 260 | ✗ | { return refMoleFrac_; } | |
| 261 | |||
| 262 | //! Returns the reference temperature. | ||
| 263 | ✗ | const Scalar refTemperature() const | |
| 264 | ✗ | { return refTemperature_; } | |
| 265 | |||
| 266 | |||
| 267 | void setTimeLoop(TimeLoopPtr timeLoop) | ||
| 268 |
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2 | { timeLoop_ = timeLoop; } |
| 269 | |||
| 270 | Scalar time() const | ||
| 271 | { return timeLoop_->time(); } | ||
| 272 | |||
| 273 | /*! | ||
| 274 | * \brief Returns the intrinsic permeability of required as input parameter | ||
| 275 | * for the Beavers-Joseph-Saffman boundary condition. | ||
| 276 | */ | ||
| 277 | Scalar permeability(const Element& element, const SubControlVolumeFace& scvf) const | ||
| 278 | { | ||
| 279 | ✗ | return couplingManager().couplingData().darcyPermeability(element, scvf); | |
| 280 | } | ||
| 281 | |||
| 282 | /*! | ||
| 283 | * \brief Returns the alpha value required as input parameter for the | ||
| 284 | * Beavers-Joseph-Saffman boundary condition. | ||
| 285 | */ | ||
| 286 | ✗ | Scalar alphaBJ(const SubControlVolumeFace& scvf) const | |
| 287 | { | ||
| 288 | ✗ | return couplingManager().problem(CouplingManager::darcyIdx).spatialParams().beaversJosephCoeffAtPos(scvf.center()); | |
| 289 | } | ||
| 290 | |||
| 291 | // \} | ||
| 292 | |||
| 293 | private: | ||
| 294 | bool onLeftBoundary_(const GlobalPosition &globalPos) const | ||
| 295 |
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7816240 | { return globalPos[0] < this->gridGeometry().bBoxMin()[0] + eps_; } |
| 296 | |||
| 297 | bool onRightBoundary_(const GlobalPosition &globalPos) const | ||
| 298 |
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8249380 | { return globalPos[0] > this->gridGeometry().bBoxMax()[0] - eps_; } |
| 299 | |||
| 300 | bool onLowerBoundary_(const GlobalPosition &globalPos) const | ||
| 301 | { return globalPos[1] < this->gridGeometry().bBoxMin()[1] + eps_; } | ||
| 302 | |||
| 303 | bool onUpperBoundary_(const GlobalPosition &globalPos) const | ||
| 304 |
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8249380 | { return globalPos[1] > this->gridGeometry().bBoxMax()[1] - eps_; } |
| 305 | |||
| 306 | //! Updates the fluid state to obtain required quantities for IC/BC | ||
| 307 | 3065786 | void updateFluidStateForBC_(FluidState& fluidState, const Scalar pressure) const | |
| 308 | { | ||
| 309 | 3065786 | fluidState.setTemperature(refTemperature()); | |
| 310 | 3065786 | fluidState.setPressure(0, pressure); | |
| 311 | 3065786 | fluidState.setSaturation(0, 1.0); | |
| 312 | 3065786 | fluidState.setMoleFraction(0, 1, refMoleFrac()); | |
| 313 | 3065786 | fluidState.setMoleFraction(0, 0, 1.0 - refMoleFrac()); | |
| 314 | |||
| 315 | typename FluidSystem::ParameterCache paramCache; | ||
| 316 | 3065786 | paramCache.updatePhase(fluidState, 0); | |
| 317 | |||
| 318 | 3065786 | const Scalar density = FluidSystem::density(fluidState, paramCache, 0); | |
| 319 | 3065786 | fluidState.setDensity(0, density); | |
| 320 | |||
| 321 | 3065786 | const Scalar molarDensity = FluidSystem::molarDensity(fluidState, paramCache, 0); | |
| 322 | 3065786 | fluidState.setMolarDensity(0, molarDensity); | |
| 323 | |||
| 324 | 3065786 | const Scalar enthalpy = FluidSystem::enthalpy(fluidState, paramCache, 0); | |
| 325 | 6131572 | fluidState.setEnthalpy(0, enthalpy); | |
| 326 | 3065786 | } | |
| 327 | |||
| 328 | //! Set the profile of the inflow velocity (horizontal direction). | ||
| 329 | const Scalar xVelocity_(const GlobalPosition &globalPos) const | ||
| 330 | { | ||
| 331 | 3065786 | const Scalar vmax = refVelocity(); | |
| 332 |
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1553360 | return 4 * vmax * (globalPos[1] - this->gridGeometry().bBoxMin()[1]) * (this->gridGeometry().bBoxMax()[1] - globalPos[1]) |
| 333 | 9197358 | / (height_() * height_()); | |
| 334 | } | ||
| 335 | |||
| 336 | // the height of the free-flow domain | ||
| 337 | const Scalar height_() const | ||
| 338 |
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2524210 | { return this->gridGeometry().bBoxMax()[1] - this->gridGeometry().bBoxMin()[1]; } |
| 339 | |||
| 340 | Scalar eps_; | ||
| 341 | |||
| 342 | Scalar refVelocity_; | ||
| 343 | Scalar refPressure_; | ||
| 344 | Scalar refMoleFrac_; | ||
| 345 | Scalar refTemperature_; | ||
| 346 | std::string problemName_; | ||
| 347 | TimeLoopPtr timeLoop_; | ||
| 348 | |||
| 349 | std::shared_ptr<CouplingManager> couplingManager_; | ||
| 350 | |||
| 351 | DiffusionCoefficientAveragingType diffCoeffAvgType_; | ||
| 352 | }; | ||
| 353 | } // end namespace Dumux | ||
| 354 | |||
| 355 | #endif | ||
| 356 |