/// Solve the pressure equation. The nonlinear equations ares
/// solved by a Newton-Raphson scheme. May throw an exception if
/// the number of iterations exceed maxiter (set in constructor).
void CompressibleTpfaPolymer::solve(const double dt,
PolymerBlackoilState& state,
WellState& well_state)
{
c_ = &state.getCellData( state.CONCENTRATION );
cmax_ = &state.getCellData( state.CMAX );
CompressibleTpfa::solve(dt, state, well_state);
}
/// @brief Computes total absorbed polymer mass over all grid cells.
/// With compressibility
/// @param[in] grid grid
/// @param[in] props fluid and rock properties.
/// @param[in] polyprops polymer properties
/// @param[in] state fluid state variable
/// @param[in] rock_comp rock compressibility (depends on pressure)
/// @return total absorbed polymer mass.
double computePolymerAdsorbed(const UnstructuredGrid& grid,
const BlackoilPropertiesInterface& props,
const Opm::PolymerProperties& polyprops,
const PolymerBlackoilState& state,
const RockCompressibility* rock_comp
)
{
const int num_cells = props.numCells();
const double rhor = polyprops.rockDensity();
std::vector<double> porosity;
if (rock_comp && rock_comp->isActive()) {
computePorosity(grid, props.porosity(), *rock_comp, state.pressure(), porosity);
} else {
porosity.assign(props.porosity(), props.porosity() + num_cells);
}
double abs_mass = 0.0;
const std::vector<double>& cmax = state.getCellData( state.CMAX );
for (int cell = 0; cell < num_cells; ++cell) {
double c_ads;
polyprops.simpleAdsorption(cmax[cell], c_ads);
abs_mass += c_ads*grid.cell_volumes[cell]*(1.0 - porosity[cell])*rhor;
}
return abs_mass;
}
SimulatorReport SimulatorCompressiblePolymer::Impl::run(SimulatorTimer& timer,
PolymerBlackoilState& state,
WellState& well_state)
{
std::vector<double> transport_src(grid_.number_of_cells);
std::vector<double> polymer_inflow_c(grid_.number_of_cells);
// Initialisation.
std::vector<double> initial_pressure;
std::vector<double> porevol;
if (rock_comp_props_ && rock_comp_props_->isActive()) {
computePorevolume(grid_, props_.porosity(), *rock_comp_props_, state.pressure(), porevol);
} else {
computePorevolume(grid_, props_.porosity(), porevol);
}
const double tot_porevol_init = std::accumulate(porevol.begin(), porevol.end(), 0.0);
std::vector<double> initial_porevol = porevol;
// Main simulation loop.
Opm::time::StopWatch pressure_timer;
double ptime = 0.0;
Opm::time::StopWatch transport_timer;
double ttime = 0.0;
Opm::time::StopWatch total_timer;
total_timer.start();
double init_surfvol[2] = { 0.0 };
double inplace_surfvol[2] = { 0.0 };
double polymass = computePolymerMass(porevol, state.saturation(), state.getCellData( state.CONCENTRATION ), poly_props_.deadPoreVol());
double polymass_adsorbed = computePolymerAdsorbed(grid_, props_, poly_props_, state, rock_comp_props_);
double init_polymass = polymass + polymass_adsorbed;
double tot_injected[2] = { 0.0 };
double tot_produced[2] = { 0.0 };
double tot_polyinj = 0.0;
double tot_polyprod = 0.0;
Opm::computeSaturatedVol(porevol, state.surfacevol(), init_surfvol);
Opm::Watercut watercut;
watercut.push(0.0, 0.0, 0.0);
Opm::WellReport wellreport;
std::vector<double> fractional_flows;
std::vector<double> well_resflows_phase;
if (wells_) {
well_resflows_phase.resize((wells_->number_of_phases)*(wells_->number_of_wells), 0.0);
wellreport.push(props_, *wells_, state.pressure(), state.surfacevol(),
state.saturation(), 0.0, well_state.bhp(), well_state.perfRates());
}
// Report timestep and (optionally) write state to disk.
timer.report(std::cout);
if (output_ && (timer.currentStepNum() % output_interval_ == 0)) {
if (output_vtk_) {
outputStateVtk(grid_, state, timer.currentStepNum(), output_dir_);
}
outputStateMatlab(grid_, state, timer.currentStepNum(), output_dir_);
}
initial_pressure = state.pressure();
// Solve pressure equation.
if (check_well_controls_) {
computeFractionalFlow(props_, poly_props_, allcells_,
state.pressure(), state.temperature(), state.surfacevol(), state.saturation(),
state.getCellData( state.CONCENTRATION ), state.getCellData( state.CMAX ) ,
fractional_flows);
wells_manager_.applyExplicitReinjectionControls(well_resflows_phase, well_resflows_phase);
}
bool well_control_passed = !check_well_controls_;
int well_control_iteration = 0;
do {
// Run solver
pressure_timer.start();
psolver_.solve(timer.currentStepLength(), state, well_state);
// Renormalize pressure if both fluids and rock are
// incompressible, and there are no pressure
// conditions (bcs or wells). It is deemed sufficient
// for now to renormalize using geometric volume
// instead of pore volume.
if (psolver_.singularPressure()) {
// Compute average pressures of previous and last
// step, and total volume.
double av_prev_press = 0.0;
double av_press = 0.0;
double tot_vol = 0.0;
const int num_cells = grid_.number_of_cells;
for (int cell = 0; cell < num_cells; ++cell) {
av_prev_press += initial_pressure[cell]*grid_.cell_volumes[cell];
av_press += state.pressure()[cell]*grid_.cell_volumes[cell];
tot_vol += grid_.cell_volumes[cell];
}
// Renormalization constant
const double ren_const = (av_prev_press - av_press)/tot_vol;
for (int cell = 0; cell < num_cells; ++cell) {
state.pressure()[cell] += ren_const;
}
const int num_wells = (wells_ == NULL) ? 0 : wells_->number_of_wells;
for (int well = 0; well < num_wells; ++well) {
well_state.bhp()[well] += ren_const;
}
}
// Stop timer and report
pressure_timer.stop();
double pt = pressure_timer.secsSinceStart();
std::cout << "Pressure solver took: " << pt << " seconds." << std::endl;
ptime += pt;
// Optionally, check if well controls are satisfied.
if (check_well_controls_) {
Opm::computePhaseFlowRatesPerWell(*wells_,
well_state.perfRates(),
fractional_flows,
well_resflows_phase);
std::cout << "Checking well conditions." << std::endl;
// For testing we set surface := reservoir
well_control_passed = wells_manager_.conditionsMet(well_state.bhp(), well_resflows_phase, well_resflows_phase);
++well_control_iteration;
if (!well_control_passed && well_control_iteration > max_well_control_iterations_) {
OPM_THROW(std::runtime_error, "Could not satisfy well conditions in " << max_well_control_iterations_ << " tries.");
}
if (!well_control_passed) {
std::cout << "Well controls not passed, solving again." << std::endl;
} else {
std::cout << "Well conditions met." << std::endl;
}
}
} while (!well_control_passed);
// Update pore volumes if rock is compressible.
if (rock_comp_props_ && rock_comp_props_->isActive()) {
initial_porevol = porevol;
computePorevolume(grid_, props_.porosity(), *rock_comp_props_, state.pressure(), porevol);
}
// Process transport sources (to include bdy terms and well flows).
Opm::computeTransportSource(props_, wells_, well_state, transport_src);
// Find inflow rate.
const double current_time = timer.simulationTimeElapsed();
double stepsize = timer.currentStepLength();
polymer_inflow_.getInflowValues(current_time, current_time + stepsize, polymer_inflow_c);
// Solve transport.
transport_timer.start();
if (num_transport_substeps_ != 1) {
stepsize /= double(num_transport_substeps_);
std::cout << "Making " << num_transport_substeps_ << " transport substeps." << std::endl;
}
double injected[2] = { 0.0 };
double produced[2] = { 0.0 };
double polyinj = 0.0;
double polyprod = 0.0;
for (int tr_substep = 0; tr_substep < num_transport_substeps_; ++tr_substep) {
tsolver_.solve(&state.faceflux()[0], initial_pressure,
state.pressure(), state.temperature(), &initial_porevol[0], &porevol[0],
&transport_src[0], &polymer_inflow_c[0], stepsize,
state.saturation(), state.surfacevol(),
state.getCellData( state.CONCENTRATION ), state.getCellData( state.CMAX ));
double substep_injected[2] = { 0.0 };
double substep_produced[2] = { 0.0 };
double substep_polyinj = 0.0;
double substep_polyprod = 0.0;
Opm::computeInjectedProduced(props_, poly_props_,
state,
transport_src, polymer_inflow_c, stepsize,
substep_injected, substep_produced,
substep_polyinj, substep_polyprod);
injected[0] += substep_injected[0];
injected[1] += substep_injected[1];
produced[0] += substep_produced[0];
produced[1] += substep_produced[1];
polyinj += substep_polyinj;
polyprod += substep_polyprod;
if (gravity_ != 0 && use_segregation_split_) {
tsolver_.solveGravity(columns_, stepsize,
state.saturation(), state.surfacevol(),
state.getCellData( state.CONCENTRATION ), state.getCellData( state.CMAX ));
}
}
transport_timer.stop();
double tt = transport_timer.secsSinceStart();
std::cout << "Transport solver took: " << tt << " seconds." << std::endl;
ttime += tt;
// Report volume balances.
Opm::computeSaturatedVol(porevol, state.surfacevol(), inplace_surfvol);
polymass = Opm::computePolymerMass(porevol, state.saturation(), state.getCellData( state.CONCENTRATION ), poly_props_.deadPoreVol());
polymass_adsorbed = Opm::computePolymerAdsorbed(grid_, props_, poly_props_,
state, rock_comp_props_);
tot_injected[0] += injected[0];
tot_injected[1] += injected[1];
tot_produced[0] += produced[0];
tot_produced[1] += produced[1];
tot_polyinj += polyinj;
tot_polyprod += polyprod;
std::cout.precision(5);
const int width = 18;
std::cout << "\nMass balance: "
" water(surfvol) oil(surfvol) polymer(kg)\n";
std::cout << " In-place: "
<< std::setw(width) << inplace_surfvol[0]
<< std::setw(width) << inplace_surfvol[1]
<< std::setw(width) << polymass << std::endl;
std::cout << " Adsorbed: "
<< std::setw(width) << 0.0
<< std::setw(width) << 0.0
<< std::setw(width) << polymass_adsorbed << std::endl;
std::cout << " Injected: "
<< std::setw(width) << injected[0]
<< std::setw(width) << injected[1]
<< std::setw(width) << polyinj << std::endl;
std::cout << " Produced: "
<< std::setw(width) << produced[0]
<< std::setw(width) << produced[1]
<< std::setw(width) << polyprod << std::endl;
std::cout << " Total inj: "
<< std::setw(width) << tot_injected[0]
<< std::setw(width) << tot_injected[1]
<< std::setw(width) << tot_polyinj << std::endl;
std::cout << " Total prod: "
<< std::setw(width) << tot_produced[0]
<< std::setw(width) << tot_produced[1]
<< std::setw(width) << tot_polyprod << std::endl;
const double balance[3] = { init_surfvol[0] - inplace_surfvol[0] - tot_produced[0] + tot_injected[0],
init_surfvol[1] - inplace_surfvol[1] - tot_produced[1] + tot_injected[1],
init_polymass - polymass - tot_polyprod + tot_polyinj - polymass_adsorbed };
std::cout << " Initial - inplace + inj - prod: "
<< std::setw(width) << balance[0]
<< std::setw(width) << balance[1]
<< std::setw(width) << balance[2]
<< std::endl;
std::cout << " Relative mass error: "
<< std::setw(width) << balance[0]/(init_surfvol[0] + tot_injected[0])
<< std::setw(width) << balance[1]/(init_surfvol[1] + tot_injected[1])
<< std::setw(width) << balance[2]/(init_polymass + tot_polyinj)
<< std::endl;
std::cout.precision(8);
watercut.push(timer.simulationTimeElapsed() + timer.currentStepLength(),
produced[0]/(produced[0] + produced[1]),
tot_produced[0]/tot_porevol_init);
if (wells_) {
wellreport.push(props_, *wells_, state.pressure(), state.surfacevol(),
state.saturation(), timer.simulationTimeElapsed() + timer.currentStepLength(),
well_state.bhp(), well_state.perfRates());
}
if (output_) {
if (output_vtk_) {
outputStateVtk(grid_, state, timer.currentStepNum(), output_dir_);
}
outputStateMatlab(grid_, state, timer.currentStepNum(), output_dir_);
outputWaterCut(watercut, output_dir_);
if (wells_) {
outputWellReport(wellreport, output_dir_);
}
}
total_timer.stop();
SimulatorReport report;
report.pressure_time = ptime;
report.transport_time = ttime;
report.total_time = total_timer.secsSinceStart();
return report;
}
/// @brief Computes injected and produced volumes of all phases,
/// and injected and produced polymer mass - in the compressible case.
/// Note 1: assumes that only the first phase is injected.
/// Note 2: assumes that transport has been done with an
/// implicit method, i.e. that the current state
/// gives the mobilities used for the preceding timestep.
/// @param[in] props fluid and rock properties.
/// @param[in] polyprops polymer properties
/// @param[in] state state variables (pressure, fluxes etc.)
/// @param[in] transport_src if < 0: total reservoir volume outflow,
/// if > 0: first phase *surface volume* inflow.
/// @param[in] inj_c injected concentration by cell
/// @param[in] dt timestep used
/// @param[out] injected must point to a valid array with P elements,
/// where P = s.size()/transport_src.size().
/// @param[out] produced must also point to a valid array with P elements.
/// @param[out] polyinj injected mass of polymer
/// @param[out] polyprod produced mass of polymer
void computeInjectedProduced(const BlackoilPropertiesInterface& props,
const Opm::PolymerProperties& polyprops,
const PolymerBlackoilState& state,
const std::vector<double>& transport_src,
const std::vector<double>& inj_c,
const double dt,
double* injected,
double* produced,
double& polyinj,
double& polyprod)
{
const int num_cells = transport_src.size();
if (props.numCells() != num_cells) {
OPM_THROW(std::runtime_error, "Size of transport_src vector does not match number of cells in props.");
}
const int np = props.numPhases();
if (int(state.saturation().size()) != num_cells*np) {
OPM_THROW(std::runtime_error, "Sizes of state vectors do not match number of cells.");
}
const std::vector<double>& press = state.pressure();
const std::vector<double>& temp = state.temperature();
const std::vector<double>& s = state.saturation();
const std::vector<double>& z = state.surfacevol();
const std::vector<double>& c = state.getCellData( state.CONCENTRATION );
const std::vector<double>& cmax = state.getCellData( state.CMAX );
std::fill(injected, injected + np, 0.0);
std::fill(produced, produced + np, 0.0);
polyinj = 0.0;
polyprod = 0.0;
std::vector<double> visc(np);
std::vector<double> kr_cell(np);
std::vector<double> mob(np);
std::vector<double> A(np*np);
std::vector<double> prod_resv_phase(np);
std::vector<double> prod_surfvol(np);
double mc;
for (int cell = 0; cell < num_cells; ++cell) {
if (transport_src[cell] > 0.0) {
// Inflowing transport source is a surface volume flux
// for the first phase.
injected[0] += transport_src[cell]*dt;
polyinj += transport_src[cell]*dt*inj_c[cell];
} else if (transport_src[cell] < 0.0) {
// Outflowing transport source is a total reservoir
// volume flux.
const double flux = -transport_src[cell]*dt;
const double* sat = &s[np*cell];
props.relperm(1, sat, &cell, &kr_cell[0], 0);
props.viscosity(1, &press[cell], &temp[cell], &z[np*cell], &cell, &visc[0], 0);
props.matrix(1, &press[cell], &temp[cell], &z[np*cell], &cell, &A[0], 0);
polyprops.effectiveMobilities(c[cell], cmax[cell], &visc[0],
&kr_cell[0], &mob[0]);
double totmob = 0.0;
for (int p = 0; p < np; ++p) {
totmob += mob[p];
}
std::fill(prod_surfvol.begin(), prod_surfvol.end(), 0.0);
for (int p = 0; p < np; ++p) {
prod_resv_phase[p] = (mob[p]/totmob)*flux;
for (int q = 0; q < np; ++q) {
prod_surfvol[q] += prod_resv_phase[p]*A[q + np*p];
}
}
for (int p = 0; p < np; ++p) {
produced[p] += prod_surfvol[p];
}
polyprops.computeMc(c[cell], mc);
polyprod += produced[0]*mc;
}
}
}
