/// @brief Computes injected and produced surface volumes of all phases.
/// 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.
/// Note 3: Gives surface volume values, not reservoir volumes
/// (as the incompressible version of the function does).
/// Also, assumes that transport_src is given in surface volumes
/// for injector terms!
/// @param[in] props fluid and rock properties.
/// @param[in] state state variables (pressure, sat, surfvol)
/// @param[in] transport_src if < 0: total resv outflow, if > 0: first phase surfv inflow
/// @param[in] dt timestep used
/// @param[out] injected must point to a valid array with P elements,
/// where P = s.size()/src.size().
/// @param[out] produced must also point to a valid array with P elements.
void computeInjectedProduced(const BlackoilPropertiesInterface& props,
const BlackoilState& state,
const std::vector<double>& transport_src,
const double dt,
double* injected,
double* produced)
{
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();
std::fill(injected, injected + np, 0.0);
std::fill(produced, produced + np, 0.0);
std::vector<double> visc(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);
for (int c = 0; c < num_cells; ++c) {
if (transport_src[c] > 0.0) {
// Inflowing transport source is a surface volume flux
// for the first phase.
injected[0] += transport_src[c]*dt;
} else if (transport_src[c] < 0.0) {
// Outflowing transport source is a total reservoir
// volume flux.
const double flux = -transport_src[c]*dt;
const double* sat = &s[np*c];
props.relperm(1, sat, &c, &mob[0], 0);
props.viscosity(1, &press[c], &temp[c], &z[np*c], &c, &visc[0], 0);
props.matrix(1, &press[c], &temp[c], &z[np*c], &c, &A[0], 0);
double totmob = 0.0;
for (int p = 0; p < np; ++p) {
mob[p] /= visc[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];
}
}
}
}
void WellReport::push(const BlackoilPropertiesInterface& props,
const Wells& wells,
const std::vector<double>& p,
const std::vector<double>& z,
const std::vector<double>& s,
const double time,
const std::vector<double>& well_bhp,
const std::vector<double>& well_perfrates)
{
// TODO: refactor, since this is almost identical to the other push().
int nw = well_bhp.size();
assert(nw == wells.number_of_wells);
int np = props.numPhases();
const int max_np = 3;
if (np > max_np) {
OPM_THROW(std::runtime_error, "WellReport for now assumes #phases <= " << max_np);
}
std::vector<double> data_now;
data_now.reserve(1 + 3*nw);
data_now.push_back(time/unit::day);
for (int w = 0; w < nw; ++w) {
data_now.push_back(well_bhp[w]/(unit::barsa));
double well_rate_total = 0.0;
double well_rate_water = 0.0;
for (int perf = wells.well_connpos[w]; perf < wells.well_connpos[w + 1]; ++perf) {
const double perf_rate = unit::convert::to(well_perfrates[perf],
unit::cubic(unit::meter)/unit::day);
well_rate_total += perf_rate;
if (perf_rate > 0.0) {
// Injection.
well_rate_water += perf_rate*wells.comp_frac[0];
} else {
// Production.
const int cell = wells.well_cells[perf];
double mob[max_np];
props.relperm(1, &s[np*cell], &cell, mob, 0);
double visc[max_np];
props.viscosity(1, &p[cell], 0, &z[np*cell], &cell, visc, 0);
double tmob = 0;
for(int i = 0; i < np; ++i) {
mob[i] /= visc[i];
tmob += mob[i];
}
const double fracflow = mob[0]/(tmob);
well_rate_water += perf_rate*fracflow;
}
}
data_now.push_back(well_rate_total);
if (well_rate_total == 0.0) {
data_now.push_back(0.0);
} else {
data_now.push_back(well_rate_water/well_rate_total);
}
}
data_.push_back(data_now);
}
/// @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;
}
}
}