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PTFlash.hpp
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// -*- mode: C++; tab-width: 4; indent-tabs-mode: nil; c-basic-offset: 4 -*-
// vi: set et ts=4 sw=4 sts=4:
/*
Copyright 2022 NORCE.
Copyright 2022 SINTEF Digital, Mathematics and Cybernetics.
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 2 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 <http://www.gnu.org/licenses/>.
Consult the COPYING file in the top-level source directory of this
module for the precise wording of the license and the list of
copyright holders.
*/
#ifndef OPM_CHI_FLASH_HPP
#define OPM_CHI_FLASH_HPP
#include <opm/material/fluidmatrixinteractions/NullMaterial.hpp>
#include <opm/material/fluidmatrixinteractions/MaterialTraits.hpp>
#include <opm/material/fluidstates/CompositionalFluidState.hpp>
#include <opm/material/densead/Evaluation.hpp>
#include <opm/material/densead/Math.hpp>
#include <opm/material/common/MathToolbox.hpp>
#include <opm/material/common/Valgrind.hpp>
#include <opm/material/Constants.hpp>
#include <opm/material/eos/CubicEOS.hpp>
#include <opm/input/eclipse/EclipseState/Compositional/CompositionalConfig.hpp>
#include <dune/common/fvector.hh>
#include <dune/common/fmatrix.hh>
#include <dune/common/classname.hh>
#include <limits>
#include <iostream>
#include <iomanip>
#include <stdexcept>
#include <type_traits>
#include <fmt/format.h>
namespace Opm {
template <class Scalar, class FluidSystem>
class PTFlash
{
static constexpr int numPhases = FluidSystem::numPhases;
static constexpr int numComponents = FluidSystem::numComponents;
enum { oilPhaseIdx = FluidSystem::oilPhaseIdx};
enum { gasPhaseIdx = FluidSystem::gasPhaseIdx};
enum { waterPhaseIdx = FluidSystem::waterPhaseIdx};
static constexpr int numMiscibleComponents = FluidSystem::numMiscibleComponents;
static constexpr int numMisciblePhases = FluidSystem::numMisciblePhases; //oil, gas
static constexpr int numEq = numMisciblePhases + numMisciblePhases * numMiscibleComponents;
using EOSType = CompositionalConfig::EOSType;
public:
template <class FluidState>
static bool solve(FluidState& fluid_state,
const std::string& twoPhaseMethod,
Scalar flash_tolerance,
const EOSType& eos_type,
int verbosity = 0)
{
using ScalarFluidState = CompositionalFluidState<Scalar, FluidSystem>;
ScalarFluidState fluid_state_scalar;
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
fluid_state_scalar.setKvalue(compIdx, Opm::getValue(fluid_state.K(compIdx) ) );
fluid_state_scalar.setMoleFraction(compIdx, Opm::getValue(fluid_state.moleFraction(compIdx) ) );
}
fluid_state_scalar.setLvalue(Opm::getValue(fluid_state.L()));
// other values need to be Scalar, but I guess the fluidstate does not support it yet.
fluid_state_scalar.setPressure(FluidSystem::oilPhaseIdx,
Opm::getValue(fluid_state.pressure(FluidSystem::oilPhaseIdx)));
fluid_state_scalar.setPressure(FluidSystem::gasPhaseIdx,
Opm::getValue(fluid_state.pressure(FluidSystem::gasPhaseIdx)));
fluid_state_scalar.setTemperature(Opm::getValue(fluid_state.temperature(0)));
const auto is_single_phase = flash_solve_scalar_(fluid_state_scalar, twoPhaseMethod, flash_tolerance, eos_type, verbosity);
// the flash solution process were performed in scalar form, after the flash calculation finishes,
// ensure that things in fluid_state_scalar is transformed to fluid_state
for (int compIdx=0; compIdx<numComponents; ++compIdx){
const auto x_i = fluid_state_scalar.moleFraction(oilPhaseIdx, compIdx);
fluid_state.setMoleFraction(oilPhaseIdx, compIdx, x_i);
const auto y_i = fluid_state_scalar.moleFraction(gasPhaseIdx, compIdx);
fluid_state.setMoleFraction(gasPhaseIdx, compIdx, y_i);
}
// we update the derivatives in fluid_state
updateDerivatives_(fluid_state_scalar, fluid_state, eos_type, is_single_phase);
return is_single_phase;
} //end solve
template <class FluidState, class ComponentVector>
static void solve(FluidState& fluid_state,
const ComponentVector& globalMolarities,
Scalar tolerance = 0.0)
{
using MaterialTraits = NullMaterialTraits<Scalar, numPhases>;
using MaterialLaw = NullMaterial<MaterialTraits>;
using MaterialLawParams = typename MaterialLaw::Params;
MaterialLawParams matParams;
solve<MaterialLaw>(fluid_state, matParams, globalMolarities, tolerance);
}
template <class Vector>
static typename Vector::field_type solveRachfordRice_g_(const Vector& K, const Vector& z, int verbosity)
{
// Find min and max K. Have to do a laborious for loop to avoid water component (where K=0)
// TODO: Replace loop with Dune::min_value() and Dune::max_value() when water component is properly handled
using field_type = typename Vector::field_type;
constexpr field_type tol = 1e-12;
constexpr int itmax = 10000;
field_type Kmin = K[0];
field_type Kmax = K[0];
for (int compIdx = 1; compIdx < numComponents; ++compIdx){
if (K[compIdx] < Kmin)
Kmin = K[compIdx];
else if (K[compIdx] >= Kmax)
Kmax = K[compIdx];
}
// Lower and upper bound for solution
auto Vmin = 1 / (1 - Kmax);
auto Vmax = 1 / (1 - Kmin);
// Initial guess
auto V = (Vmin + Vmax)/2;
// Print initial guess and header
if (verbosity == 3 || verbosity == 4) {
std::cout << "Initial guess " << numComponents << "c : V = " << V << " and [Vmin, Vmax] = [" << Vmin << ", " << Vmax << "]" << std::endl;
std::cout << std::setw(10) << "Iteration" << std::setw(16) << "abs(step)" << std::setw(16) << "V" << std::endl;
}
// Newton-Raphson loop
for (int iteration = 1; iteration < itmax; ++iteration) {
// Calculate function and derivative values
field_type denum = 0.0;
field_type r = 0.0;
for (int compIdx = 0; compIdx < numComponents; ++compIdx){
auto dK = K[compIdx] - 1.0;
auto a = z[compIdx] * dK;
auto b = (1 + V * dK);
r += a/b;
denum += z[compIdx] * (dK*dK) / (b*b);
}
auto delta = r / denum;
V += delta;
// Check if V is within the bounds, and if not, we apply bisection method
if (V < Vmin || V > Vmax)
{
// Print info
if (verbosity == 3 || verbosity == 4) {
std::cout << "V = " << V << " is not within the the range [Vmin, Vmax], solve using Bisection method!" << std::endl;
}
// Run bisection
// TODO: This is required for some cases. Not clear why
// since the objective function should be monotone with a
// single zero between the Lmin/Lmax interval defined by
// K-values.
decltype(Vmax) Lmin = 1.0;
decltype(Vmin) Lmax = 0.0;
auto L = bisection_g_(K, Lmin, Lmax, z, verbosity);
// Print final result
if (verbosity >= 1) {
std::cout << "Rachford-Rice (Bisection) converged to final solution L = " << L << std::endl;
}
return L;
}
// Print iteration info
if (verbosity == 3 || verbosity == 4) {
std::cout << std::setw(10) << iteration << std::setw(16) << Opm::abs(delta) << std::setw(16) << V << std::endl;
}
// Check for convergence
if ( Opm::abs(r) < tol ) {
auto L = 1 - V;
// Should we make sure the range of L is within (0, 1)?
// Print final result
if (verbosity >= 1) {
std::cout << "Rachford-Rice converged to final solution L = " << L << std::endl;
}
return L;
}
}
// Throw error if Rachford-Rice fails
throw std::runtime_error(" Rachford-Rice did not converge within maximum number of iterations" );
}
// performing the flash calculation, which is done with Scalar without touching derivatives
template <typename FluidState>
static bool flash_solve_scalar_(FluidState& fluid_state,
const std::string& twoPhaseMethod,
const Scalar flash_tolerance,
const EOSType& eos_type,
const int verbosity = 0)
{
// Do a stability test to check if cell is is_single_phase-phase (do for all cells the first time).
bool is_stable = false;
auto L_scalar = fluid_state.L();
using ScalarVector = Dune::FieldVector<Scalar, numComponents>;
ScalarVector K_scalar, z_scalar;
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
K_scalar[compIdx] = fluid_state.K(compIdx);
z_scalar[compIdx] = fluid_state.moleFraction(compIdx);
}
if ( L_scalar <= 0 || L_scalar == 1 ) {
if (verbosity >= 1) {
std::cout << "Perform stability test (L <= 0 or L == 1)!" << std::endl;
}
phaseStabilityTest_(is_stable, K_scalar, fluid_state, z_scalar, eos_type, verbosity);
}
if (verbosity >= 1) {
std::cout << "Inputs after stability test are K = [" << K_scalar << "], L = [" << L_scalar << "], z = [" << z_scalar << "], P = " << fluid_state.pressure(0) << ", and T = " << fluid_state.temperature(0) << std::endl;
}
// TODO: we do not need two variables is_stable and is_single_hase, while lacking a good name
// TODO: from the later code, is good if we knows whether single_phase_gas or single_phase_oil here
const bool is_single_phase = is_stable;
// Update the composition if cell is two-phase
if ( !is_single_phase ) {
// Rachford Rice equation to get initial L for composition solver
L_scalar = solveRachfordRice_g_(K_scalar, z_scalar, verbosity);
flash_2ph(z_scalar, twoPhaseMethod, K_scalar, L_scalar, fluid_state, flash_tolerance, eos_type, verbosity);
} else {
// Cell is one-phase. Use Li's phase labeling method to see if it's liquid or vapor
L_scalar = li_single_phase_label_(fluid_state, z_scalar, verbosity);
}
fluid_state.setLvalue(L_scalar);
return is_single_phase;
}
template <class Vector>
static typename Vector::field_type bisection_g_(const Vector& K, typename Vector::field_type Lmin,
typename Vector::field_type Lmax, const Vector& z, int verbosity)
{
// Calculate for g(Lmin) for first comparison with gMid = g(L)
typename Vector::field_type gLmin = rachfordRice_g_(K, Lmin, z);
// Print new header
if (verbosity >= 3) {
std::cout << std::setw(10) << "Iteration" << std::setw(16) << "g(Lmid)" << std::setw(16) << "L" << std::endl;
}
constexpr int max_it = 10000;
auto closeLmaxLmin = [](double max_v, double min_v) {
return Opm::abs(max_v - min_v) / 2. < 1e-10;
// what if max_v < min_v?
};
// Bisection loop
if (closeLmaxLmin(Lmax, Lmin) ){
throw std::runtime_error(fmt::format("Strange bisection with Lmax {} and Lmin {}?", Lmax, Lmin));
}
for (int iteration = 0; iteration < max_it; ++iteration){
// New midpoint
auto L = (Lmin + Lmax) / 2;
auto gMid = rachfordRice_g_(K, L, z);
// std::cout << ">>> Lmin = " << Lmin << "g(Lmin) = " << gLmin << " L = " << L << " g(L) = " << gMid << std::endl;
if (verbosity == 3 || verbosity == 4) {
std::cout << std::setw(10) << iteration << std::setw(16) << gMid << std::setw(16) << L << std::endl;
}
// Check if midpoint fulfills g=0 or L - Lmin is sufficiently small
if (Opm::abs(gMid) < 1e-16 || closeLmaxLmin(Lmax, Lmin)){
return L;
}
// Else we repeat with midpoint being either Lmin og Lmax (depending on the signs).
else if (Dune::sign(gMid) != Dune::sign(gLmin)) {
// gMid has different sign as gLmin, so we set L as the new Lmax
Lmax = L;
}
else {
// gMid and gLmin have same sign so we set L as the new Lmin
Lmin = L;
gLmin = gMid;
}
}
throw std::runtime_error(" Rachford-Rice bisection failed with " + std::to_string(max_it) + " iterations!");
}
template <class Vector, class FlashFluidState>
static typename Vector::field_type li_single_phase_label_(const FlashFluidState& fluid_state, const Vector& z, int verbosity)
{
// Calculate intermediate sum
typename Vector::field_type sumVz = 0.0;
for (int compIdx=0; compIdx<numComponents; ++compIdx){
// Get component information
const auto& V_crit = FluidSystem::criticalVolume(compIdx);
// Sum calculation
sumVz += (V_crit * z[compIdx]);
}
// Calculate approximate (pseudo) critical temperature using Li's method
typename Vector::field_type Tc_est = 0.0;
for (int compIdx=0; compIdx<numComponents; ++compIdx){
// Get component information
const auto& V_crit = FluidSystem::criticalVolume(compIdx);
const auto& T_crit = FluidSystem::criticalTemperature(compIdx);
// Sum calculation
Tc_est += (V_crit * T_crit * z[compIdx] / sumVz);
}
// Get temperature
const auto& T = fluid_state.temperature(0);
// If temperature is below estimated critical temperature --> phase = liquid; else vapor
typename Vector::field_type L;
if (T < Tc_est) {
// Liquid
L = 1.0;
// Print
if (verbosity >= 1) {
std::cout << "Cell is single-phase, liquid (L = 1.0) due to Li's phase labeling method giving T < Tc_est (" << T << " < " << Tc_est << ")!" << std::endl;
}
}
else {
// Vapor
L = 0.0;
// Print
if (verbosity >= 1) {
std::cout << "Cell is single-phase, vapor (L = 0.0) due to Li's phase labeling method giving T >= Tc_est (" << T << " >= " << Tc_est << ")!" << std::endl;
}
}
return L;
}
template <class FlashFluidState, class ComponentVector>
static void phaseStabilityTest_(bool& isStable, ComponentVector& K, FlashFluidState& fluid_state, const ComponentVector& z, const EOSType& eos_type, int verbosity)
{
// Declarations
bool isTrivialL, isTrivialV;
ComponentVector x, y;
typename FlashFluidState::Scalar S_l, S_v;
ComponentVector K0 = K;
ComponentVector K1 = K;
// Check for vapour instable phase
if (verbosity == 3 || verbosity == 4) {
std::cout << "Stability test for vapor phase:" << std::endl;
}
checkStability_(fluid_state, isTrivialV, K0, y, S_v, z, /*isGas=*/true, eos_type, verbosity);
bool V_unstable = (S_v < (1.0 + 1e-5)) || isTrivialV;
// Check for liquids stable phase
if (verbosity == 3 || verbosity == 4) {
std::cout << "Stability test for liquid phase:" << std::endl;
}
checkStability_(fluid_state, isTrivialL, K1, x, S_l, z, /*isGas=*/false, eos_type, verbosity);
bool L_stable = (S_l < (1.0 + 1e-5)) || isTrivialL;
// L-stable means success in making liquid, V-unstable means no success in making vapour
isStable = L_stable && V_unstable;
if (isStable) {
// Single phase, i.e. phase composition is equivalent to the global composition
// Update fluid_state with mole fraction
for (int compIdx=0; compIdx<numComponents; ++compIdx){
fluid_state.setMoleFraction(gasPhaseIdx, compIdx, z[compIdx]);
fluid_state.setMoleFraction(oilPhaseIdx, compIdx, z[compIdx]);
}
}
// If not stable: use the mole fractions from Michelsen's test to update K
else {
for (int compIdx = 0; compIdx<numComponents; ++compIdx) {
K[compIdx] = y[compIdx] / x[compIdx];
}
}
}
protected:
template <class FlashFluidState>
static typename FlashFluidState::Scalar wilsonK_(const FlashFluidState& fluid_state, int compIdx)
{
const auto& acf = FluidSystem::acentricFactor(compIdx);
const auto& T_crit = FluidSystem::criticalTemperature(compIdx);
const auto& T = fluid_state.temperature(0);
const auto& p_crit = FluidSystem::criticalPressure(compIdx);
const auto& p = fluid_state.pressure(0); //for now assume no capillary pressure
const auto& tmp = Opm::exp(5.3727 * (1+acf) * (1-T_crit/T)) * (p_crit/p);
return tmp;
}
template <class Vector>
static typename Vector::field_type rachfordRice_g_(const Vector& K, typename Vector::field_type L, const Vector& z)
{
typename Vector::field_type g=0;
for (int compIdx=0; compIdx<numComponents; ++compIdx){
g += (z[compIdx]*(K[compIdx]-1))/(K[compIdx]-L*(K[compIdx]-1));
}
return g;
}
template <class Vector>
static typename Vector::field_type rachfordRice_dg_dL_(const Vector& K, const typename Vector::field_type L, const Vector& z)
{
typename Vector::field_type dg=0;
for (int compIdx=0; compIdx<numComponents; ++compIdx){
dg += (z[compIdx]*(K[compIdx]-1)*(K[compIdx]-1))/((K[compIdx]-L*(K[compIdx]-1))*(K[compIdx]-L*(K[compIdx]-1)));
}
return dg;
}
template <class FlashFluidState, class ComponentVector>
static void checkStability_(const FlashFluidState& fluid_state, bool& isTrivial, ComponentVector& K, ComponentVector& xy_loc,
typename FlashFluidState::Scalar& S_loc, const ComponentVector& z, bool isGas, const EOSType& eos_type,
int verbosity)
{
using FlashEval = typename FlashFluidState::Scalar;
using CubicEOS = typename Opm::CubicEOS<Scalar, FluidSystem>;
// Declarations
FlashFluidState fluid_state_fake = fluid_state;
FlashFluidState fluid_state_global = fluid_state;
// Setup output
if (verbosity >= 3) {
std::cout << std::setw(10) << "Iteration" << std::setw(16) << "K-Norm" << std::setw(16) << "R-Norm" << std::endl;
}
// Michelsens stability test.
// Make two fake phases "inside" one phase and check for positive volume
for (int i = 0; i < 20000; ++i) {
S_loc = 0.0;
if (isGas) {
for (int compIdx=0; compIdx<numComponents; ++compIdx){
xy_loc[compIdx] = K[compIdx] * z[compIdx];
S_loc += xy_loc[compIdx];
}
for (int compIdx=0; compIdx<numComponents; ++compIdx){
xy_loc[compIdx] /= S_loc;
fluid_state_fake.setMoleFraction(gasPhaseIdx, compIdx, xy_loc[compIdx]);
}
}
else {
for (int compIdx=0; compIdx<numComponents; ++compIdx){
xy_loc[compIdx] = z[compIdx]/K[compIdx];
S_loc += xy_loc[compIdx];
}
for (int compIdx=0; compIdx<numComponents; ++compIdx){
xy_loc[compIdx] /= S_loc;
fluid_state_fake.setMoleFraction(oilPhaseIdx, compIdx, xy_loc[compIdx]);
}
}
int phaseIdx = (isGas ? static_cast<int>(gasPhaseIdx) : static_cast<int>(oilPhaseIdx));
int phaseIdx2 = (isGas ? static_cast<int>(oilPhaseIdx) : static_cast<int>(gasPhaseIdx));
// TODO: not sure the following makes sense
for (int compIdx=0; compIdx<numComponents; ++compIdx){
fluid_state_global.setMoleFraction(phaseIdx2, compIdx, z[compIdx]);
}
typename FluidSystem::template ParameterCache<FlashEval> paramCache_fake(eos_type);
paramCache_fake.updatePhase(fluid_state_fake, phaseIdx);
typename FluidSystem::template ParameterCache<FlashEval> paramCache_global(eos_type);
paramCache_global.updatePhase(fluid_state_global, phaseIdx2);
//fugacity for fake phases each component
for (int compIdx=0; compIdx<numComponents; ++compIdx){
auto phiFake = CubicEOS::computeFugacityCoefficient(fluid_state_fake, paramCache_fake, phaseIdx, compIdx);
auto phiGlobal = CubicEOS::computeFugacityCoefficient(fluid_state_global, paramCache_global, phaseIdx2, compIdx);
fluid_state_fake.setFugacityCoefficient(phaseIdx, compIdx, phiFake);
fluid_state_global.setFugacityCoefficient(phaseIdx2, compIdx, phiGlobal);
}
ComponentVector R;
for (int compIdx=0; compIdx<numComponents; ++compIdx){
if (isGas){
auto fug_fake = fluid_state_fake.fugacity(phaseIdx, compIdx);
auto fug_global = fluid_state_global.fugacity(phaseIdx2, compIdx);
auto fug_ratio = fug_global / fug_fake;
R[compIdx] = fug_ratio / S_loc;
}
else{
auto fug_fake = fluid_state_fake.fugacity(phaseIdx, compIdx);
auto fug_global = fluid_state_global.fugacity(phaseIdx2, compIdx);
auto fug_ratio = fug_fake / fug_global;
R[compIdx] = fug_ratio * S_loc;
}
}
for (int compIdx=0; compIdx<numComponents; ++compIdx){
K[compIdx] *= R[compIdx];
}
Scalar R_norm = 0.0;
Scalar K_norm = 0.0;
for (int compIdx=0; compIdx<numComponents; ++compIdx){
auto a = Opm::getValue(R[compIdx]) - 1.0;
auto b = Opm::log(Opm::getValue(K[compIdx]));
R_norm += a*a;
K_norm += b*b;
}
// Print iteration info
if (verbosity >= 3) {
std::cout << std::setw(10) << i << std::setw(16) << K_norm << std::setw(16) << R_norm << std::endl;
}
// Check convergence
isTrivial = (K_norm < 1e-5);
if (isTrivial || R_norm < 1e-10)
return;
//todo: make sure that no mole fraction is smaller than 1e-8 ?
//todo: take care of water!
}
throw std::runtime_error(" Stability test did not converge");
}//end checkStability
// TODO: basically FlashFluidState and ComponentVector are both depending on the one Scalar type
template <class FlashFluidState, class ComponentVector>
static void computeLiquidVapor_(FlashFluidState& fluid_state, typename FlashFluidState::Scalar& L, ComponentVector& K, const ComponentVector& z)
{
// Calculate x and y, and normalize
ComponentVector x;
ComponentVector y;
typename FlashFluidState::Scalar sumx=0;
typename FlashFluidState::Scalar sumy=0;
for (int compIdx=0; compIdx<numComponents; ++compIdx){
x[compIdx] = z[compIdx]/(L + (1-L)*K[compIdx]);
sumx += x[compIdx];
y[compIdx] = (K[compIdx]*z[compIdx])/(L + (1-L)*K[compIdx]);
sumy += y[compIdx];
}
x /= sumx;
y /= sumy;
for (int compIdx=0; compIdx<numComponents; ++compIdx){
fluid_state.setMoleFraction(oilPhaseIdx, compIdx, x[compIdx]);
fluid_state.setMoleFraction(gasPhaseIdx, compIdx, y[compIdx]);
}
}
template <class FluidState, class ComponentVector>
static void flash_2ph(const ComponentVector& z_scalar,
const std::string& flash_2p_method,
ComponentVector& K_scalar,
typename FluidState::Scalar& L_scalar,
FluidState& fluid_state_scalar,
const Scalar flash_tolerance,
const EOSType& eos_type,
int verbosity = 0) {
if (verbosity >= 1) {
std::cout << "Cell is two-phase! Solve Rachford-Rice with initial K = [" << K_scalar << "]" << std::endl;
}
// Calculate composition using nonlinear solver
// Newton
bool converged = false;
if (flash_2p_method == "newton") {
if (verbosity >= 1) {
std::cout << "Calculate composition using Newton." << std::endl;
}
converged = newtonComposition_(K_scalar, L_scalar, fluid_state_scalar, z_scalar, flash_tolerance, eos_type, verbosity);
} else if (flash_2p_method == "ssi") {
// Successive substitution
if (verbosity >= 1) {
std::cout << "Calculate composition using Succcessive Substitution." << std::endl;
}
converged = successiveSubstitutionComposition_(K_scalar, L_scalar, fluid_state_scalar, z_scalar, false, flash_tolerance, eos_type, verbosity);
} else if (flash_2p_method == "ssi+newton") {
converged = successiveSubstitutionComposition_(K_scalar, L_scalar, fluid_state_scalar, z_scalar, true, flash_tolerance, eos_type, verbosity);
if (!converged) {
converged = newtonComposition_(K_scalar, L_scalar, fluid_state_scalar, z_scalar, flash_tolerance, eos_type, verbosity);
}
} else {
throw std::logic_error("unknown two phase flash method " + flash_2p_method + " is specified");
}
if (!converged) {
throw std::runtime_error("flash calculation did not get converged with " + flash_2p_method);
}
}
template <class FlashFluidState, class ComponentVector>
static bool newtonComposition_(ComponentVector& K,
typename FlashFluidState::Scalar& L,
FlashFluidState& fluid_state,
const ComponentVector& z,
const Scalar tolerance,
const EOSType& eos_type,
int verbosity)
{
// Note: due to the need for inverse flash update for derivatives, the following two can be different
// Looking for a good way to organize them
constexpr size_t num_equations = numMisciblePhases * numMiscibleComponents + 1;
constexpr size_t num_primary_variables = numMisciblePhases * numMiscibleComponents + 1;
using NewtonVector = Dune::FieldVector<Scalar, num_equations>;
using NewtonMatrix = Dune::FieldMatrix<Scalar, num_equations, num_primary_variables>;
NewtonVector soln(0.);
NewtonVector res(0.);
NewtonMatrix jac (0.);
// Compute x and y from K, L and Z
computeLiquidVapor_(fluid_state, L, K, z);
// Print initial condition
if (verbosity >= 1) {
std::cout << " the current L is " << Opm::getValue(L) << std::endl;
std::cout << "Initial guess: x = [";
for (int compIdx=0; compIdx<numComponents; ++compIdx){
if (compIdx < numComponents - 1)
std::cout << fluid_state.moleFraction(oilPhaseIdx, compIdx) << " ";
else
std::cout << fluid_state.moleFraction(oilPhaseIdx, compIdx);
}
std::cout << "], y = [";
for (int compIdx=0; compIdx<numComponents; ++compIdx){
if (compIdx < numComponents - 1)
std::cout << fluid_state.moleFraction(gasPhaseIdx, compIdx) << " ";
else
std::cout << fluid_state.moleFraction(gasPhaseIdx, compIdx);
}
std::cout << "], and " << "L = " << L << std::endl;
}
// Print header
if (verbosity == 2 || verbosity == 4) {
std::cout << std::setw(10) << "Iteration" << std::setw(16) << "Norm2(step)" << std::setw(16) << "Norm2(Residual)" << std::endl;
}
// AD type
using Eval = DenseAd::Evaluation<Scalar, num_primary_variables>;
// TODO: we might need to use numMiscibleComponents here
std::vector<Eval> x(numComponents), y(numComponents);
Eval l;
// TODO: I might not need to set soln anything here.
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
x[compIdx] = Eval(fluid_state.moleFraction(oilPhaseIdx, compIdx), compIdx);
const unsigned idx = compIdx + numComponents;
y[compIdx] = Eval(fluid_state.moleFraction(gasPhaseIdx, compIdx), idx);
}
l = Eval(L, num_primary_variables - 1);
// it is created for the AD calculation for the flash calculation
CompositionalFluidState<Eval, FluidSystem> flash_fluid_state;
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
flash_fluid_state.setMoleFraction(FluidSystem::oilPhaseIdx, compIdx, x[compIdx]);
flash_fluid_state.setMoleFraction(FluidSystem::gasPhaseIdx, compIdx, y[compIdx]);
// TODO: should we use wilsonK_ here?
flash_fluid_state.setKvalue(compIdx, y[compIdx] / x[compIdx]);
}
flash_fluid_state.setLvalue(l);
// other values need to be Scalar, but I guess the fluid_state does not support it yet.
flash_fluid_state.setPressure(FluidSystem::oilPhaseIdx,
fluid_state.pressure(FluidSystem::oilPhaseIdx));
flash_fluid_state.setPressure(FluidSystem::gasPhaseIdx,
fluid_state.pressure(FluidSystem::gasPhaseIdx));
// TODO: not sure whether we need to set the saturations
flash_fluid_state.setSaturation(FluidSystem::gasPhaseIdx,
fluid_state.saturation(FluidSystem::gasPhaseIdx));
flash_fluid_state.setSaturation(FluidSystem::oilPhaseIdx,
fluid_state.saturation(FluidSystem::oilPhaseIdx));
flash_fluid_state.setTemperature(fluid_state.temperature(0));
using ParamCache = typename FluidSystem::template ParameterCache<typename CompositionalFluidState<Eval, FluidSystem>::Scalar>;
ParamCache paramCache(eos_type);
for (unsigned phaseIdx = 0; phaseIdx < numMisciblePhases; ++phaseIdx) {
paramCache.updatePhase(flash_fluid_state, phaseIdx);
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
// TODO: will phi here carry the correct derivatives?
Eval phi = FluidSystem::fugacityCoefficient(flash_fluid_state, paramCache, phaseIdx, compIdx);
flash_fluid_state.setFugacityCoefficient(phaseIdx, compIdx, phi);
}
}
bool converged = false;
unsigned iter = 0;
constexpr unsigned max_iter = 1000;
while (iter < max_iter) {
assembleNewton_<CompositionalFluidState<Eval, FluidSystem>, ComponentVector, num_primary_variables, num_equations>
(flash_fluid_state, z, jac, res);
if (verbosity >= 1) {
std::cout << " newton residual is " << res.two_norm() << std::endl;
}
converged = res.two_norm() < tolerance;
if (converged) {
break;
}
jac.solve(soln, res);
constexpr Scalar damping_factor = 1.0;
// updating x and y
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
x[compIdx] -= soln[compIdx] * damping_factor;
y[compIdx] -= soln[compIdx + numComponents] * damping_factor;
}
l -= soln[num_equations - 1] * damping_factor;
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
flash_fluid_state.setMoleFraction(FluidSystem::oilPhaseIdx, compIdx, x[compIdx]);
flash_fluid_state.setMoleFraction(FluidSystem::gasPhaseIdx, compIdx, y[compIdx]);
// TODO: should we use wilsonK_ here?
flash_fluid_state.setKvalue(compIdx, y[compIdx] / x[compIdx]);
}
flash_fluid_state.setLvalue(l);
for (unsigned phaseIdx = 0; phaseIdx < numMisciblePhases; ++phaseIdx) {
paramCache.updatePhase(flash_fluid_state, phaseIdx);
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
Eval phi = FluidSystem::fugacityCoefficient(flash_fluid_state, paramCache, phaseIdx, compIdx);
flash_fluid_state.setFugacityCoefficient(phaseIdx, compIdx, phi);
}
}
++iter;
}
if (verbosity >= 1) {
for (unsigned i = 0; i < num_equations; ++i) {
for (unsigned j = 0; j < num_primary_variables; ++j) {
std::cout << " " << jac[i][j];
}
std::cout << std::endl;
}
std::cout << std::endl;
}
if (!converged) {
throw std::runtime_error(" Newton composition update did not converge within maxIterations " + std::to_string(max_iter));
}
// fluid_state is scalar, we need to update all the values for fluid_state here
for (unsigned idx = 0; idx < numComponents; ++idx) {
const auto x_i = Opm::getValue(flash_fluid_state.moleFraction(oilPhaseIdx, idx));
fluid_state.setMoleFraction(FluidSystem::oilPhaseIdx, idx, x_i);
const auto y_i = Opm::getValue(flash_fluid_state.moleFraction(gasPhaseIdx, idx));
fluid_state.setMoleFraction(FluidSystem::gasPhaseIdx, idx, y_i);
const auto K_i = Opm::getValue(flash_fluid_state.K(idx));
fluid_state.setKvalue(idx, K_i);
// TODO: not sure we need K and L here, because they are in the flash_fluid_state anyway.
K[idx] = K_i;
}
L = Opm::getValue(l);
fluid_state.setLvalue(L);
return converged;
}
// TODO: the interface will need to refactor for later usage
template<typename FlashFluidState, typename ComponentVector, size_t num_primary, size_t num_equation >
static void assembleNewton_(const FlashFluidState& fluid_state,
const ComponentVector& global_composition,
Dune::FieldMatrix<double, num_equation, num_primary>& jac,
Dune::FieldVector<double, num_equation>& res)
{
using Eval = DenseAd::Evaluation<double, num_primary>;
std::vector<Eval> x(numComponents), y(numComponents);
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
x[compIdx] = fluid_state.moleFraction(oilPhaseIdx, compIdx);
y[compIdx] = fluid_state.moleFraction(gasPhaseIdx, compIdx);
}
const Eval& l = fluid_state.L();
// TODO: clearing zero whether necessary?
jac = 0.;
res = 0.;
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
{
// z - L*x - (1-L) * y
auto local_res = -global_composition[compIdx] + l * x[compIdx] + (1 - l) * y[compIdx];
res[compIdx] = Opm::getValue(local_res);
for (unsigned i = 0; i < num_primary; ++i) {
jac[compIdx][i] = local_res.derivative(i);
}
}
{
// f_liquid - f_vapor = 0
auto local_res = (fluid_state.fugacity(oilPhaseIdx, compIdx) -
fluid_state.fugacity(gasPhaseIdx, compIdx));
res[compIdx + numComponents] = Opm::getValue(local_res);
for (unsigned i = 0; i < num_primary; ++i) {
jac[compIdx + numComponents][i] = local_res.derivative(i);
}
}
}
// sum(x) - sum(y) = 0
Eval sumx = 0.;
Eval sumy = 0.;
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
sumx += x[compIdx];
sumy += y[compIdx];
}
auto local_res = sumx - sumy;
res[num_equation - 1] = Opm::getValue(local_res);
for (unsigned i = 0; i < num_primary; ++i) {
jac[num_equation - 1][i] = local_res.derivative(i);
}
}
template <typename FlashFluidStateScalar, typename FluidState>
static void updateDerivatives_(const FlashFluidStateScalar& fluid_state_scalar,
FluidState& fluid_state,
const EOSType& eos_type,
bool is_single_phase)
{
if(!is_single_phase)
updateDerivativesTwoPhase_(fluid_state_scalar, fluid_state, eos_type);
else
updateDerivativesSinglePhase_(fluid_state_scalar, fluid_state);
}
template <typename FlashFluidStateScalar, typename FluidState>
static void updateDerivativesTwoPhase_(const FlashFluidStateScalar& fluid_state_scalar,
FluidState& fluid_state,
const EOSType& eos_type)
{
using InputEval = typename FluidState::Scalar;
using ComponentVector = Dune::FieldVector<InputEval, numComponents>;
ComponentVector z;
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
z[compIdx] = fluid_state.moleFraction(compIdx);
}
// getting the secondary Jocobian matrix
constexpr size_t num_equations = numMisciblePhases * numMiscibleComponents + 1;
constexpr size_t secondary_num_pv = numComponents + 1; // pressure, z for all the components
using SecondaryEval = Opm::DenseAd::Evaluation<double, secondary_num_pv>; // three z and one pressure
using SecondaryComponentVector = Dune::FieldVector<SecondaryEval, numComponents>;
using SecondaryFlashFluidState = Opm::CompositionalFluidState<SecondaryEval, FluidSystem>;
SecondaryFlashFluidState secondary_fluid_state;
SecondaryComponentVector secondary_z;
// p and z are the primary variables here
// pressure
const SecondaryEval sec_p = SecondaryEval(fluid_state_scalar.pressure(FluidSystem::oilPhaseIdx), 0);
secondary_fluid_state.setPressure(FluidSystem::oilPhaseIdx, sec_p);
secondary_fluid_state.setPressure(FluidSystem::gasPhaseIdx, sec_p);
// set the temperature // TODO: currently we are not considering the temperature derivatives
secondary_fluid_state.setTemperature(Opm::getValue(fluid_state_scalar.temperature(0)));
for (unsigned idx = 0; idx < numComponents; ++idx) {
secondary_z[idx] = SecondaryEval(Opm::getValue(z[idx]), idx + 1);
}
// set up the mole fractions
for (unsigned idx = 0; idx < numComponents; ++idx) {
// TODO: double checking that fluid_state_scalar returns a scalar here
const auto x_i = fluid_state_scalar.moleFraction(oilPhaseIdx, idx);
secondary_fluid_state.setMoleFraction(FluidSystem::oilPhaseIdx, idx, x_i);
const auto y_i = fluid_state_scalar.moleFraction(gasPhaseIdx, idx);
secondary_fluid_state.setMoleFraction(FluidSystem::gasPhaseIdx, idx, y_i);
// TODO: double checking make sure those are consistent
const auto K_i = fluid_state_scalar.K(idx);
secondary_fluid_state.setKvalue(idx, K_i);
}
const auto L = fluid_state_scalar.L();
secondary_fluid_state.setLvalue(L);
// TODO: Do we need to update the saturations?
// compositions
// TODO: we probably can simplify SecondaryFlashFluidState::Scalar
using SecondaryParamCache = typename FluidSystem::template ParameterCache<typename SecondaryFlashFluidState::Scalar>;
SecondaryParamCache secondary_param_cache(eos_type);
for (unsigned phase_idx = 0; phase_idx < numMisciblePhases; ++phase_idx) {
secondary_param_cache.updatePhase(secondary_fluid_state, phase_idx);
for (unsigned comp_idx = 0; comp_idx < numComponents; ++comp_idx) {
SecondaryEval phi = FluidSystem::fugacityCoefficient(secondary_fluid_state, secondary_param_cache, phase_idx, comp_idx);
secondary_fluid_state.setFugacityCoefficient(phase_idx, comp_idx, phi);
}
}
using SecondaryNewtonVector = Dune::FieldVector<Scalar, num_equations>;
using SecondaryNewtonMatrix = Dune::FieldMatrix<Scalar, num_equations, secondary_num_pv>;
SecondaryNewtonMatrix sec_jac;
SecondaryNewtonVector sec_res;
//use the regular equations
assembleNewton_<SecondaryFlashFluidState, SecondaryComponentVector, secondary_num_pv, num_equations>
(secondary_fluid_state, secondary_z, sec_jac, sec_res);
// assembly the major matrix here
// primary variables are x, y and L
constexpr size_t primary_num_pv = numMisciblePhases * numMiscibleComponents + 1;
using PrimaryEval = Opm::DenseAd::Evaluation<double, primary_num_pv>;
using PrimaryComponentVector = Dune::FieldVector<double, numComponents>;
using PrimaryFlashFluidState = Opm::CompositionalFluidState<PrimaryEval, FluidSystem>;
PrimaryFlashFluidState primary_fluid_state;
// primary_z is not needed, because we use z will be okay here
PrimaryComponentVector primary_z;
for (unsigned comp_idx = 0; comp_idx < numComponents; ++comp_idx) {
primary_z[comp_idx] = Opm::getValue(z[comp_idx]);
}
for (unsigned comp_idx = 0; comp_idx < numComponents; ++comp_idx) {
const auto x_ii = PrimaryEval(fluid_state_scalar.moleFraction(oilPhaseIdx, comp_idx), comp_idx);
primary_fluid_state.setMoleFraction(oilPhaseIdx, comp_idx, x_ii);
const unsigned idx = comp_idx + numComponents;
const auto y_ii = PrimaryEval(fluid_state_scalar.moleFraction(gasPhaseIdx, comp_idx), idx);
primary_fluid_state.setMoleFraction(gasPhaseIdx, comp_idx, y_ii);
primary_fluid_state.setKvalue(comp_idx, y_ii / x_ii);
}
PrimaryEval l;
l = PrimaryEval(fluid_state_scalar.L(), primary_num_pv - 1);
primary_fluid_state.setLvalue(l);
primary_fluid_state.setPressure(oilPhaseIdx, fluid_state_scalar.pressure(oilPhaseIdx));
primary_fluid_state.setPressure(gasPhaseIdx, fluid_state_scalar.pressure(gasPhaseIdx));
primary_fluid_state.setTemperature(fluid_state_scalar.temperature(0));
// TODO: is PrimaryFlashFluidState::Scalar> PrimaryEval here?
using PrimaryParamCache = typename FluidSystem::template ParameterCache<typename PrimaryFlashFluidState::Scalar>;
PrimaryParamCache primary_param_cache(eos_type);
for (unsigned phase_idx = 0; phase_idx < numMisciblePhases; ++phase_idx) {
primary_param_cache.updatePhase(primary_fluid_state, phase_idx);
for (unsigned comp_idx = 0; comp_idx < numComponents; ++comp_idx) {
PrimaryEval phi = FluidSystem::fugacityCoefficient(primary_fluid_state, primary_param_cache, phase_idx, comp_idx);
primary_fluid_state.setFugacityCoefficient(phase_idx, comp_idx, phi);
}
}
using PrimaryNewtonVector = Dune::FieldVector<Scalar, num_equations>;
using PrimaryNewtonMatrix = Dune::FieldMatrix<Scalar, num_equations, primary_num_pv>;
PrimaryNewtonVector pri_res;
PrimaryNewtonMatrix pri_jac;
//use the regular equations
assembleNewton_<PrimaryFlashFluidState, PrimaryComponentVector, primary_num_pv, num_equations>
(primary_fluid_state, primary_z, pri_jac, pri_res);
// the following code does not compile with DUNE2.6
// SecondaryNewtonMatrix xx;
// pri_jac.solve(xx, sec_jac);
pri_jac.invert();
sec_jac.template leftmultiply<PrimaryNewtonMatrix>(pri_jac);
ComponentVector x(numComponents), y(numComponents);
InputEval L_eval = L;
// use the chainrule (and using partial instead of total
// derivatives, DF / Dp = dF / dp + dF / ds * ds/dp.
// where p is the primary variables and s the secondary variables. We then obtain
// ds / dp = -inv(dF / ds)*(DF / Dp)
const auto p_l = fluid_state.pressure(FluidSystem::oilPhaseIdx);
const auto p_v = fluid_state.pressure(FluidSystem::gasPhaseIdx);
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
x[compIdx] = fluid_state_scalar.moleFraction(FluidSystem::oilPhaseIdx,compIdx);//;z[compIdx] * 1. / (L + (1 - L) * K[compIdx]);
y[compIdx] = fluid_state_scalar.moleFraction(FluidSystem::gasPhaseIdx,compIdx);//;x[compIdx] * K[compIdx];
}
// then we try to set the derivatives for x, y and L against P and x.
// p_l and p_v are the same here, in the future, there might be slightly more complicated scenarios when capillary
// pressure joins
constexpr size_t num_deri = InputEval::numVars;
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
std::vector<double> deri(num_deri, 0.);
// derivatives from P
for (unsigned idx = 0; idx < num_deri; ++idx) {
deri[idx] = -sec_jac[compIdx][0] * p_l.derivative(idx);
}
for (unsigned cIdx = 0; cIdx < numComponents; ++cIdx) {
const double pz = -sec_jac[compIdx][cIdx + 1];
const auto& zi = z[cIdx];
for (unsigned idx = 0; idx < num_deri; ++idx) {
deri[idx] += pz * zi.derivative(idx);
}
}
for (unsigned idx = 0; idx < num_deri; ++idx) {
x[compIdx].setDerivative(idx, deri[idx]);
}
// handling y
for (unsigned idx = 0; idx < num_deri; ++idx) {
deri[idx] = -sec_jac[compIdx + numComponents][0] * p_v.derivative(idx);
}
for (unsigned cIdx = 0; cIdx < numComponents; ++cIdx) {
const double pz = -sec_jac[compIdx + numComponents][cIdx + 1];
const auto& zi = z[cIdx];
for (unsigned idx = 0; idx < num_deri; ++idx) {
deri[idx] += pz * zi.derivative(idx);
}
}
for (unsigned idx = 0; idx < num_deri; ++idx) {
y[compIdx].setDerivative(idx, deri[idx]);
}
// handling derivatives of L
std::vector<double> deriL(num_deri, 0.);
for (unsigned idx = 0; idx < num_deri; ++idx) {
deriL[idx] = -sec_jac[2 * numComponents][0] * p_v.derivative(idx);
}
for (unsigned cIdx = 0; cIdx < numComponents; ++cIdx) {
const double pz = -sec_jac[2 * numComponents][cIdx + 1];
const auto& zi = z[cIdx];
for (unsigned idx = 0; idx < num_deri; ++idx) {
deriL[idx] += pz * zi.derivative(idx);
}
}
for (unsigned idx = 0; idx < num_deri; ++idx) {
L_eval.setDerivative(idx, deriL[idx]);
}
}
// set up the mole fractions
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
fluid_state.setMoleFraction(FluidSystem::oilPhaseIdx, compIdx, x[compIdx]);
fluid_state.setMoleFraction(FluidSystem::gasPhaseIdx, compIdx, y[compIdx]);
}
fluid_state.setLvalue(L_eval);
} //end updateDerivativesTwoPhase
template <typename FlashFluidStateScalar, typename FluidState>
static void updateDerivativesSinglePhase_(const FlashFluidStateScalar& fluid_state_scalar,
FluidState& fluid_state)
{
using InputEval = typename FluidState::Scalar;
// L_eval is converted from a scalar, so all derivatives are zero at this point
InputEval L_eval = fluid_state_scalar.L();;
// for single phase situation, x = y = z;
// and L_eval have all zero derivatives
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx) {
fluid_state.setMoleFraction(FluidSystem::oilPhaseIdx, compIdx, fluid_state.moleFraction(compIdx) );
fluid_state.setMoleFraction(FluidSystem::gasPhaseIdx, compIdx, fluid_state.moleFraction(compIdx) );
}
fluid_state.setLvalue(L_eval);
} //end updateDerivativesSinglePhase
// TODO: or use typename FlashFluidState::Scalar
template <class FlashFluidState, class ComponentVector>
static bool successiveSubstitutionComposition_(ComponentVector& K,
typename ComponentVector::field_type& L,
FlashFluidState& fluid_state,
const ComponentVector& z,
const bool newton_afterwards,
const Scalar flash_tolerance,
const EOSType& eos_type,
const int verbosity)
{
// Determine max. iterations based on if it will be used as a standalone flash or as a pre-process to Newton (or other) method.
const int maxIterations = newton_afterwards ? 5 : 100;
// Store cout format before manipulation
std::ios_base::fmtflags f(std::cout.flags());
// Print initial guess
if (verbosity >= 1)
std::cout << "Initial guess: K = [" << K << "] and L = " << L << std::endl;
if (verbosity == 2 || verbosity == 4) {
// Print header
int fugWidth = (numComponents * 12)/2;
int convWidth = fugWidth + 7;
std::cout << std::setw(10) << "Iteration" << std::setw(fugWidth) << "fL/fV" << std::setw(convWidth) << "norm2(fL/fv-1)" << std::endl;
}
//
// Successive substitution loop
//
for (int i=0; i < maxIterations; ++i){
// Compute (normalized) liquid and vapor mole fractions
computeLiquidVapor_(fluid_state, L, K, z);
// Calculate fugacity coefficient
using ParamCache = typename FluidSystem::template ParameterCache<typename FlashFluidState::Scalar>;
ParamCache paramCache(eos_type);
for (int phaseIdx=0; phaseIdx<numMisciblePhases; ++phaseIdx){
paramCache.updatePhase(fluid_state, phaseIdx);
for (int compIdx=0; compIdx<numComponents; ++compIdx){
auto phi = FluidSystem::fugacityCoefficient(fluid_state, paramCache, phaseIdx, compIdx);
fluid_state.setFugacityCoefficient(phaseIdx, compIdx, phi);
}
}
// Calculate fugacity ratio
ComponentVector newFugRatio;
ComponentVector convFugRatio;
for (int compIdx=0; compIdx<numComponents; ++compIdx){
newFugRatio[compIdx] = fluid_state.fugacity(oilPhaseIdx, compIdx)/fluid_state.fugacity(gasPhaseIdx, compIdx);
convFugRatio[compIdx] = newFugRatio[compIdx] - 1.0;
}
// Print iteration info
if (verbosity >= 2) {
int prec = 5;
int fugWidth = (prec + 3);
int convWidth = prec + 9;
std::cout << std::defaultfloat;
std::cout << std::fixed;
std::cout << std::setw(5) << i;
std::cout << std::setw(fugWidth);
std::cout << std::setprecision(prec);
std::cout << newFugRatio;
std::cout << std::scientific;
std::cout << std::setw(convWidth) << convFugRatio.two_norm() << std::endl;
}
// Check convergence
if (convFugRatio.two_norm() < flash_tolerance) {
// Restore cout format
std::cout.flags(f);
// Print info
if (verbosity >= 1) {
std::cout << "Solution converged to the following result :" << std::endl;
std::cout << "x = [";
for (int compIdx = 0; compIdx < numComponents; ++compIdx) {
if (compIdx < numComponents - 1)
std::cout << fluid_state.moleFraction(oilPhaseIdx, compIdx) << " ";
else
std::cout << fluid_state.moleFraction(oilPhaseIdx, compIdx);
}
std::cout << "]" << std::endl;
std::cout << "y = [";
for (int compIdx = 0; compIdx < numComponents; ++compIdx) {
if (compIdx < numComponents - 1)
std::cout << fluid_state.moleFraction(gasPhaseIdx, compIdx) << " ";
else
std::cout << fluid_state.moleFraction(gasPhaseIdx, compIdx);
}
std::cout << "]" << std::endl;
std::cout << "K = [" << K << "]" << std::endl;
std::cout << "L = " << L << std::endl;
}
// Restore cout format format
return true;
}
// If convergence is not met, K is updated in a successive substitution manner
else {
// Update K
for (int compIdx=0; compIdx<numComponents; ++compIdx){
K[compIdx] *= newFugRatio[compIdx];
}
// Solve Rachford-Rice to get L from updated K
L = solveRachfordRice_g_(K, z, 0);
}
}
// did not get converged. check whether we will do more newton later afterward
{
const std::string msg = fmt::format("Successive substitution composition update did not converge within maxIterations {}.", maxIterations);
if (!newton_afterwards) {
throw std::runtime_error(msg);
} else if (verbosity > 0) {
std::cout << msg << std::endl;
}
}
return false;
}
};//end PTFlash
} // namespace Opm
#endif
CompositionalFluidState.hpp
Represents all relevant thermodynamic quantities of a multi-phase, multi-component fluid system assum...
Constants.hpp
Evaluation.hpp
Representation of an evaluation of a function and its derivatives w.r.t.
MaterialTraits.hpp
This file contains helper classes for the material laws.
MathToolbox.hpp
A traits class which provides basic mathematical functions for arbitrary scalar floating point values...
Math.hpp
A number of commonly used algebraic functions for the localized OPM automatic differentiation (AD) fr...
NullMaterial.hpp
Implements a dummy linear saturation-capillary pressure relation which just disables capillary pressu...
Valgrind.hpp
Some templates to wrap the valgrind client request macros.
Opm::CompositionalFluidState
Represents all relevant thermodynamic quantities of a multi-phase, multi-component fluid system assum...
Definition CompositionalFluidState.hpp:48
Opm::NullMaterialTraits
A generic traits class which does not provide any indices.
Definition MaterialTraits.hpp:45
Opm::NullMaterial
Implements a dummy linear saturation-capillary pressure relation which just disables capillary pressu...
Definition NullMaterial.hpp:46
Opm::PTFlash
Determines the phase compositions, pressures and saturations given the total mass of all components f...
Definition PTFlash.hpp:65
Opm::PTFlash::solve
static bool solve(FluidState &fluid_state, const std::string &twoPhaseMethod, Scalar flash_tolerance, const EOSType &eos_type, int verbosity=0)
Calculates the fluid state from the global mole fractions of the components and the phase pressures.
Definition PTFlash.hpp:83
Opm::PTFlash::solve
static void solve(FluidState &fluid_state, const ComponentVector &globalMolarities, Scalar tolerance=0.0)
Calculates the chemical equilibrium from the component fugacities in a phase.
Definition PTFlash.hpp:131
Opm
This class implements a small container which holds the transmissibility mulitpliers for all the face...
Definition Exceptions.hpp:30