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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-FileCopyrightText: 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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2 | 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 | refTemperature_ = getParamFromGroup<Scalar>(this->paramGroup(), "Problem.RefTemperature"); |
| 72 |
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2 | Scalar refRelativeHumidity = getParamFromGroup<Scalar>(this->paramGroup(), "Problem.RefRelHumidity"); |
| 73 | |||
| 74 | |||
| 75 |
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2 | diffCoeffAvgType_ = StokesDarcyCouplingOptions::stringToEnum(DiffusionCoefficientAveragingType{}, |
| 76 |
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2 | getParamFromGroup<std::string>(this->paramGroup(), "Problem.InterfaceDiffusionCoefficientAvg")); |
| 77 |
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4 | problemName_ = getParam<std::string>("Vtk.OutputName") + "_" + getParamFromGroup<std::string>(this->paramGroup(), "Problem.Name"); |
| 78 | |||
| 79 | 2 | FluidState fluidState; | |
| 80 |
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2 | fluidState.setPressure(FluidSystem::phase0Idx, refPressure_); |
| 81 |
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2 | fluidState.setTemperature(refTemperature_); |
| 82 |
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2 | const auto h2oIdx = FluidSystem::compIdx(FluidSystem::MultiPhaseFluidSystem::H2OIdx); |
| 83 | 2 | Scalar vapPressure = FluidSystem::vaporPressure(fluidState, h2oIdx); | |
| 84 | 2 | refMoleFrac_ = refRelativeHumidity * vapPressure / refPressure_; | |
| 85 | 2 | } | |
| 86 | |||
| 87 | /*! | ||
| 88 | * \name Problem parameters | ||
| 89 | */ | ||
| 90 | // \{ | ||
| 91 | |||
| 92 | /*! | ||
| 93 | * \brief The problem name. | ||
| 94 | */ | ||
| 95 | 2 | const std::string& name() const | |
| 96 | { | ||
| 97 |
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2 | return problemName_; |
| 98 | } | ||
| 99 | |||
| 100 | /*! | ||
| 101 | * \brief Returns the sources within the domain. | ||
| 102 | * | ||
| 103 | * \param globalPos The global position | ||
| 104 | */ | ||
| 105 | 3111632 | NumEqVector sourceAtPos(const GlobalPosition &globalPos) const | |
| 106 |
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5456744 | { return NumEqVector(0.0); } |
| 107 | |||
| 108 | // \} | ||
| 109 | /*! | ||
| 110 | * \name Boundary conditions | ||
| 111 | */ | ||
| 112 | // \{ | ||
| 113 | |||
| 114 | /*! | ||
| 115 | * \brief Specifies which kind of boundary condition should be | ||
| 116 | * used for which equation on a given boundary segment. | ||
| 117 | * | ||
| 118 | * \param element The finite element | ||
| 119 | * \param scvf The sub control volume face | ||
| 120 | */ | ||
| 121 | 1653922 | BoundaryTypes boundaryTypes(const Element& element, | |
| 122 | const SubControlVolumeFace& scvf) const | ||
| 123 | { | ||
| 124 |
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1653922 | BoundaryTypes values; |
| 125 | |||
| 126 |
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1653922 | const auto& globalPos = scvf.center(); |
| 127 | |||
| 128 | #if NONISOTHERMAL | ||
| 129 | 1034768 | values.setNeumann(Indices::energyEqIdx); | |
| 130 | #endif | ||
| 131 | |||
| 132 |
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1653922 | if (onUpperBoundary_(globalPos) || onLeftBoundary_(globalPos)) |
| 133 | { | ||
| 134 | 749667 | values.setDirichlet(Indices::velocityXIdx); | |
| 135 | 749667 | values.setDirichlet(Indices::velocityYIdx); | |
| 136 | 749667 | values.setNeumann(Indices::conti0EqIdx); | |
| 137 | 749667 | values.setNeumann(Indices::conti0EqIdx + 1); | |
| 138 | } | ||
| 139 | |||
| 140 |
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1653922 | if (onRightBoundary_(globalPos)) |
| 141 | { | ||
| 142 | 575807 | values.setDirichlet(Indices::pressureIdx); | |
| 143 | 575807 | values.setOutflow(Indices::conti0EqIdx + 1); | |
| 144 | |||
| 145 | #if NONISOTHERMAL | ||
| 146 | 357480 | values.setOutflow(Indices::energyEqIdx); | |
| 147 | #endif | ||
| 148 | } | ||
| 149 | |||
| 150 | 3307844 | if (couplingManager().isCoupledEntity(CouplingManager::stokesIdx, scvf)) | |
| 151 | { | ||
| 152 | 328448 | values.setCouplingNeumann(Indices::conti0EqIdx); | |
| 153 | 328448 | values.setCouplingNeumann(Indices::conti0EqIdx + 1); | |
| 154 | 328448 | values.setCouplingNeumann(Indices::momentumYBalanceIdx); | |
| 155 | 328448 | values.setBeaversJoseph(Indices::momentumXBalanceIdx); | |
| 156 | } | ||
| 157 | 1653922 | return values; | |
| 158 | } | ||
| 159 | |||
| 160 | /*! | ||
| 161 | * \brief Evaluates the boundary conditions for a Dirichlet control volume. | ||
| 162 | */ | ||
| 163 | 371086 | PrimaryVariables dirichletAtPos(const GlobalPosition& pos) const | |
| 164 | { | ||
| 165 | PrimaryVariables values(0.0); | ||
| 166 |
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371086 | values = initialAtPos(pos); |
| 167 | |||
| 168 | return values; | ||
| 169 | } | ||
| 170 | |||
| 171 | /*! | ||
| 172 | * \brief Evaluates the boundary conditions for a Neumann control volume. | ||
| 173 | * | ||
| 174 | * \param element The element for which the Neumann boundary condition is set | ||
| 175 | * \param fvGeometry The fvGeometry | ||
| 176 | * \param elemVolVars The element volume variables | ||
| 177 | * \param elemFaceVars The element face variables | ||
| 178 | * \param scvf The boundary sub control volume face | ||
| 179 | */ | ||
| 180 | 194723 | NumEqVector neumann(const Element& element, | |
| 181 | const FVElementGeometry& fvGeometry, | ||
| 182 | const ElementVolumeVariables& elemVolVars, | ||
| 183 | const ElementFaceVariables& elemFaceVars, | ||
| 184 | const SubControlVolumeFace& scvf) const | ||
| 185 | { | ||
| 186 | 194723 | PrimaryVariables values(0.0); | |
| 187 | 194723 | const auto& globalPos = scvf.dofPosition(); | |
| 188 | 194723 | const auto& scv = fvGeometry.scv(scvf.insideScvIdx()); | |
| 189 | |||
| 190 | 194723 | FluidState fluidState; | |
| 191 | 194723 | updateFluidStateForBC_(fluidState, elemVolVars[scv].pressure()); | |
| 192 | |||
| 193 | 194723 | const Scalar density = useMoles ? fluidState.molarDensity(0) : fluidState.density(0); | |
| 194 | 194723 | const Scalar xVelocity = xVelocity_(globalPos); | |
| 195 | |||
| 196 | 194723 | if (onLeftBoundary_(globalPos)) | |
| 197 | { | ||
| 198 | // rho*v*X at inflow | ||
| 199 | 74101 | values[Indices::conti0EqIdx + 1] = -xVelocity * density * refMoleFrac(); | |
| 200 | 74101 | values[Indices::conti0EqIdx] = -xVelocity * density * (1.0 - refMoleFrac()); | |
| 201 | |||
| 202 | #if NONISOTHERMAL | ||
| 203 | 42220 | values[Indices::energyEqIdx] = -xVelocity * fluidState.density(0) * fluidState.enthalpy(0); | |
| 204 | #endif | ||
| 205 | } | ||
| 206 | |||
| 207 | 303944 | if(couplingManager().isCoupledEntity(CouplingManager::stokesIdx, scvf)) | |
| 208 | { | ||
| 209 | 85502 | values[Indices::momentumYBalanceIdx] = couplingManager().couplingData().momentumCouplingCondition(element, fvGeometry, elemVolVars, elemFaceVars, scvf); | |
| 210 | |||
| 211 | 85502 | const auto massFlux = couplingManager().couplingData().massCouplingCondition(element, fvGeometry, elemVolVars, elemFaceVars, scvf, diffCoeffAvgType_); | |
| 212 | 85502 | values[Indices::conti0EqIdx] = massFlux[0]; | |
| 213 | 85502 | values[Indices::conti0EqIdx + 1] = massFlux[1]; | |
| 214 | |||
| 215 | #if NONISOTHERMAL | ||
| 216 | 48356 | values[Indices::energyEqIdx] = couplingManager().couplingData().energyCouplingCondition(element, fvGeometry, elemVolVars, elemFaceVars, scvf, diffCoeffAvgType_); | |
| 217 | #endif | ||
| 218 | |||
| 219 | } | ||
| 220 | 194723 | return values; | |
| 221 | } | ||
| 222 | |||
| 223 | // \} | ||
| 224 | |||
| 225 | //! Get the coupling manager | ||
| 226 | 2353145 | const CouplingManager& couplingManager() const | |
| 227 | 1934147 | { return *couplingManager_; } | |
| 228 | |||
| 229 | /*! | ||
| 230 | * \name Volume terms | ||
| 231 | */ | ||
| 232 | // \{ | ||
| 233 | |||
| 234 | /*! | ||
| 235 | * \brief Evaluates the initial value for a control volume. | ||
| 236 | * | ||
| 237 | * \param globalPos The global position | ||
| 238 | */ | ||
| 239 | 2880182 | PrimaryVariables initialAtPos(const GlobalPosition &globalPos) const | |
| 240 | { | ||
| 241 | 2880182 | FluidState fluidState; | |
| 242 | 2880182 | updateFluidStateForBC_(fluidState, refPressure()); | |
| 243 | |||
| 244 | 2880182 | const Scalar density = FluidSystem::density(fluidState, 0); | |
| 245 | |||
| 246 | 2880182 | PrimaryVariables values(0.0); | |
| 247 | 2880182 | values[Indices::pressureIdx] = refPressure() + density*this->gravity()[1]*(globalPos[1] - this->gridGeometry().bBoxMin()[1]); | |
| 248 | 2880182 | values[Indices::conti0EqIdx + 1] = refMoleFrac(); | |
| 249 | 2880182 | values[Indices::velocityXIdx] = xVelocity_(globalPos); | |
| 250 | |||
| 251 | #if NONISOTHERMAL | ||
| 252 | 1584172 | values[Indices::temperatureIdx] = refTemperature(); | |
| 253 | #endif | ||
| 254 | |||
| 255 | 2880182 | return values; | |
| 256 | } | ||
| 257 | |||
| 258 | //! Returns the reference velocity. | ||
| 259 | 3074905 | const Scalar refVelocity() const | |
| 260 | 3074905 | { return refVelocity_ ;} | |
| 261 | |||
| 262 | //! Returns the reference pressure. | ||
| 263 | 5760364 | const Scalar refPressure() const | |
| 264 | 2880182 | { return refPressure_; } | |
| 265 | |||
| 266 | //! Returns the reference mole fraction. | ||
| 267 | 9104093 | const Scalar refMoleFrac() const | |
| 268 | 74101 | { return refMoleFrac_; } | |
| 269 | |||
| 270 | //! Returns the reference temperature. | ||
| 271 | 4659077 | const Scalar refTemperature() const | |
| 272 | 4659077 | { return refTemperature_; } | |
| 273 | |||
| 274 | |||
| 275 | 2 | void setTimeLoop(TimeLoopPtr timeLoop) | |
| 276 |
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2 | { timeLoop_ = timeLoop; } |
| 277 | |||
| 278 | Scalar time() const | ||
| 279 | { return timeLoop_->time(); } | ||
| 280 | |||
| 281 | /*! | ||
| 282 | * \brief Returns the intrinsic permeability of required as input parameter | ||
| 283 | * for the Beavers-Joseph-Saffman boundary condition. | ||
| 284 | */ | ||
| 285 | 142570 | Scalar permeability(const Element& element, const SubControlVolumeFace& scvf) const | |
| 286 | { | ||
| 287 | 142570 | return couplingManager().couplingData().darcyPermeability(element, scvf); | |
| 288 | } | ||
| 289 | |||
| 290 | /*! | ||
| 291 | * \brief Returns the alpha value required as input parameter for the | ||
| 292 | * Beavers-Joseph-Saffman boundary condition. | ||
| 293 | */ | ||
| 294 |
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142570 | Scalar alphaBJ(const SubControlVolumeFace& scvf) const |
| 295 | { | ||
| 296 |
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142570 | return couplingManager().problem(CouplingManager::darcyIdx).spatialParams().beaversJosephCoeffAtPos(scvf.center()); |
| 297 | } | ||
| 298 | |||
| 299 | // \} | ||
| 300 | |||
| 301 | private: | ||
| 302 |
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1411368 | bool onLeftBoundary_(const GlobalPosition &globalPos) const |
| 303 |
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1411368 | { return globalPos[0] < this->gridGeometry().bBoxMin()[0] + eps_; } |
| 304 | |||
| 305 |
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1653922 | bool onRightBoundary_(const GlobalPosition &globalPos) const |
| 306 |
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1653922 | { return globalPos[0] > this->gridGeometry().bBoxMax()[0] - eps_; } |
| 307 | |||
| 308 | bool onLowerBoundary_(const GlobalPosition &globalPos) const | ||
| 309 | { return globalPos[1] < this->gridGeometry().bBoxMin()[1] + eps_; } | ||
| 310 | |||
| 311 |
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1653922 | bool onUpperBoundary_(const GlobalPosition &globalPos) const |
| 312 |
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1653922 | { return globalPos[1] > this->gridGeometry().bBoxMax()[1] - eps_; } |
| 313 | |||
| 314 | //! Updates the fluid state to obtain required quantities for IC/BC | ||
| 315 | 3074905 | void updateFluidStateForBC_(FluidState& fluidState, const Scalar pressure) const | |
| 316 | { | ||
| 317 | 3074905 | fluidState.setTemperature(refTemperature()); | |
| 318 | 3074905 | fluidState.setPressure(0, pressure); | |
| 319 | 3074905 | fluidState.setSaturation(0, 1.0); | |
| 320 | 3074905 | fluidState.setMoleFraction(0, 1, refMoleFrac()); | |
| 321 | 3074905 | fluidState.setMoleFraction(0, 0, 1.0 - refMoleFrac()); | |
| 322 | |||
| 323 | typename FluidSystem::ParameterCache paramCache; | ||
| 324 | 3074905 | paramCache.updatePhase(fluidState, 0); | |
| 325 | |||
| 326 | 3074905 | const Scalar density = FluidSystem::density(fluidState, paramCache, 0); | |
| 327 | 3074905 | fluidState.setDensity(0, density); | |
| 328 | |||
| 329 | 3074905 | const Scalar molarDensity = FluidSystem::molarDensity(fluidState, paramCache, 0); | |
| 330 | 3074905 | fluidState.setMolarDensity(0, molarDensity); | |
| 331 | |||
| 332 | 3074905 | const Scalar enthalpy = FluidSystem::enthalpy(fluidState, paramCache, 0); | |
| 333 | 3074905 | fluidState.setEnthalpy(0, enthalpy); | |
| 334 | 3074905 | } | |
| 335 | |||
| 336 | //! Set the profile of the inflow velocity (horizontal direction). | ||
| 337 | 3074905 | const Scalar xVelocity_(const GlobalPosition &globalPos) const | |
| 338 | { | ||
| 339 | 3074905 | const Scalar vmax = refVelocity(); | |
| 340 |
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194723 | return 4 * vmax * (globalPos[1] - this->gridGeometry().bBoxMin()[1]) * (this->gridGeometry().bBoxMax()[1] - globalPos[1]) |
| 341 | 3074905 | / (height_() * height_()); | |
| 342 | } | ||
| 343 | |||
| 344 | // the height of the free-flow domain | ||
| 345 | 3074905 | const Scalar height_() const | |
| 346 |
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194723 | { return this->gridGeometry().bBoxMax()[1] - this->gridGeometry().bBoxMin()[1]; } |
| 347 | |||
| 348 | Scalar eps_; | ||
| 349 | |||
| 350 | Scalar refVelocity_; | ||
| 351 | Scalar refPressure_; | ||
| 352 | Scalar refMoleFrac_; | ||
| 353 | Scalar refTemperature_; | ||
| 354 | std::string problemName_; | ||
| 355 | TimeLoopPtr timeLoop_; | ||
| 356 | |||
| 357 | std::shared_ptr<CouplingManager> couplingManager_; | ||
| 358 | |||
| 359 | DiffusionCoefficientAveragingType diffCoeffAvgType_; | ||
| 360 | }; | ||
| 361 | } // end namespace Dumux | ||
| 362 | |||
| 363 | #endif | ||
| 364 |