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https://github.com/OPM/opm-simulators.git
synced 2025-02-25 18:55:30 -06:00
Changed computation of polymer production. Added functionalities for compressible case.
This commit is contained in:
@@ -339,11 +339,11 @@ namespace Opm
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&transport_src[0], stepsize, inflow_c,
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&transport_src[0], stepsize, inflow_c,
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state.saturation(), state.surfacevol(),
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state.saturation(), state.surfacevol(),
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state.concentration(), state.maxconcentration());
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state.concentration(), state.maxconcentration());
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Opm::computeInjectedProduced(props_, poly_props_,
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// Computeinjectedproduced function does not take into account polymer.
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Opm::computeInjectedProduced(props_,
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state.pressure(), state.surfacevol(), state.saturation(),
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state.pressure(), state.surfacevol(), state.saturation(),
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transport_src, stepsize, injected, produced);
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state.concentration(), state.maxconcentration(),
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transport_src, stepsize, inflow_c, injected, produced,
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polyinj, polyprod);
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if (gravity_ != 0 && use_segregation_split_) {
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if (gravity_ != 0 && use_segregation_split_) {
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tsolver_.solveGravity(columns_, stepsize,
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tsolver_.solveGravity(columns_, stepsize,
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state.saturation(), state.surfacevol(),
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state.saturation(), state.surfacevol(),
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@@ -92,7 +92,7 @@ namespace Opm
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/// @brief Computes injected and produced volumes of all phases,
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/// @brief Computes injected and produced volumes of all phases,
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/// and injeced and produced polymer mass.
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/// and injected and produced polymer mass.
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/// Note 1: assumes that only the first phase is injected.
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/// Note 1: assumes that only the first phase is injected.
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/// Note 2: assumes that transport has been done with an
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/// Note 2: assumes that transport has been done with an
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/// implicit method, i.e. that the current state
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/// implicit method, i.e. that the current state
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@@ -101,6 +101,7 @@ namespace Opm
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/// @param[in] polyprops polymer properties
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/// @param[in] polyprops polymer properties
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/// @param[in] s saturation values (for all P phases)
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/// @param[in] s saturation values (for all P phases)
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/// @param[in] c polymer concentration
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/// @param[in] c polymer concentration
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/// @param[in] cmax polymer maximum concentration
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/// @param[in] src if < 0: total outflow, if > 0: first phase inflow.
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/// @param[in] src if < 0: total outflow, if > 0: first phase inflow.
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/// @param[in] dt timestep used
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/// @param[in] dt timestep used
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/// @param[in] inj_c injected concentration
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/// @param[in] inj_c injected concentration
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@@ -134,6 +135,7 @@ namespace Opm
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const double* visc = props.viscosity();
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const double* visc = props.viscosity();
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std::vector<double> kr_cell(np);
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std::vector<double> kr_cell(np);
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double mob[2];
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double mob[2];
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double mc;
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for (int cell = 0; cell < num_cells; ++cell) {
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for (int cell = 0; cell < num_cells; ++cell) {
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if (src[cell] > 0.0) {
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if (src[cell] > 0.0) {
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injected[0] += src[cell]*dt;
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injected[0] += src[cell]*dt;
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@@ -148,11 +150,89 @@ namespace Opm
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for (int p = 0; p < np; ++p) {
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for (int p = 0; p < np; ++p) {
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produced[p] += (mob[p]/totmob)*flux;
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produced[p] += (mob[p]/totmob)*flux;
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}
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}
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polyprod += (mob[0]/totmob)*flux*c[cell]; // TODO check this term.
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polyprops.computeMc(c[cell], mc);
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polyprod += (mob[0]/totmob)*flux*mc;
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}
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}
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}
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}
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}
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}
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/// @brief Computes injected and produced volumes of all phases,
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/// and injected and produced polymer mass - in the compressible case.
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/// Note 1: assumes that only the first phase is injected.
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/// Note 2: assumes that transport has been done with an
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/// implicit method, i.e. that the current state
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/// gives the mobilities used for the preceding timestep.
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/// @param[in] props fluid and rock properties.
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/// @param[in] polyprops polymer properties
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/// @param[in] press pressure (one value per cell)
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/// @param[in] z surface-volume values (for all P phases)
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/// @param[in] s saturation values (for all P phases)
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/// @param[in] c polymer concentration
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/// @param[in] cmax polymer maximum concentration
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/// @param[in] src if < 0: total outflow, if > 0: first phase inflow.
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/// @param[in] dt timestep used
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/// @param[in] inj_c injected concentration
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///
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/// @param[out] injected must point to a valid array with P elements,
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/// where P = s.size()/src.size().
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/// @param[out] produced must also point to a valid array with P elements.
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/// @param[out] polyinj injected mass of polymer
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/// @param[out] polyprod produced mass of polymer
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void computeInjectedProduced(const BlackoilPropertiesInterface& props,
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const Opm::PolymerProperties& polyprops,
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const std::vector<double>& press,
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const std::vector<double>& z,
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const std::vector<double>& s,
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const std::vector<double>& c,
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const std::vector<double>& cmax,
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const std::vector<double>& src,
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const double dt,
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const double inj_c,
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double* injected,
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double* produced,
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double& polyinj,
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double& polyprod)
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{
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const int num_cells = src.size();
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const int np = s.size()/src.size();
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if (int(s.size()) != num_cells*np) {
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THROW("Sizes of s and src vectors do not match.");
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}
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std::fill(injected, injected + np, 0.0);
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std::fill(produced, produced + np, 0.0);
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polyinj = 0.0;
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polyprod = 0.0;
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std::vector<double> visc(np);
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std::vector<double> kr_cell(np);
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std::vector<double> mob(np);
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double mc;
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for (int cell = 0; cell < num_cells; ++cell) {
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if (src[cell] > 0.0) {
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injected[0] += src[cell]*dt;
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polyinj += src[cell]*dt*inj_c;
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} else if (src[cell] < 0.0) {
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const double flux = -src[cell]*dt;
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const double* sat = &s[np*cell];
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props.relperm(1, sat, &cell, &kr_cell[0], 0);
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props.viscosity(1, &press[cell], &z[np*cell], &cell, &visc[0], 0);
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polyprops.effectiveMobilities(c[cell], cmax[cell], &visc[0],
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&kr_cell[0], &mob[0]);
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double totmob = 0.0;
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for (int p = 0; p < np; ++p) {
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totmob += mob[p];
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}
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for (int p = 0; p < np; ++p) {
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produced[p] += (mob[p]/totmob)*flux;
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}
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polyprops.computeMc(c[cell], mc);
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polyprod += (mob[0]/totmob)*flux*mc;
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}
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}
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}
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/// @brief Computes total polymer mass over all grid cells.
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/// @brief Computes total polymer mass over all grid cells.
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/// @param[in] pv the pore volume by cell.
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/// @param[in] pv the pore volume by cell.
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@@ -97,6 +97,44 @@ namespace Opm
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double& polyinj,
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double& polyinj,
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double& polyprod);
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double& polyprod);
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/// @brief Computes injected and produced volumes of all phases,
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/// and injected and produced polymer mass - in the compressible case.
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/// Note 1: assumes that only the first phase is injected.
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/// Note 2: assumes that transport has been done with an
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/// implicit method, i.e. that the current state
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/// gives the mobilities used for the preceding timestep.
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/// @param[in] props fluid and rock properties.
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/// @param[in] polyprops polymer properties
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/// @param[in] press pressure (one value per cell)
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/// @param[in] z surface-volume values (for all P phases)
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/// @param[in] s saturation values (for all P phases)
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/// @param[in] c polymer concentration
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/// @param[in] cmax polymer maximum concentration
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/// @param[in] src if < 0: total outflow, if > 0: first phase inflow.
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/// @param[in] dt timestep used
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/// @param[in] inj_c injected concentration
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///
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/// @param[out] injected must point to a valid array with P elements,
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/// where P = s.size()/src.size().
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/// @param[out] produced must also point to a valid array with P elements.
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/// @param[out] polyinj injected mass of polymer
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/// @param[out] polyprod produced mass of polymer
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void computeInjectedProduced(const BlackoilPropertiesInterface& props,
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const Opm::PolymerProperties& polyprops,
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const std::vector<double>& press,
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const std::vector<double>& z,
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const std::vector<double>& s,
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const std::vector<double>& c,
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const std::vector<double>& cmax,
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const std::vector<double>& src,
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const double dt,
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const double inj_c,
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double* injected,
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double* produced,
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double& polyinj,
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double& polyprod);
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/// @brief Computes total (free) polymer mass over all grid cells.
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/// @brief Computes total (free) polymer mass over all grid cells.
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/// @param[in] pv the pore volume by cell.
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/// @param[in] pv the pore volume by cell.
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/// @param[in] s saturation values (for all P phases)
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/// @param[in] s saturation values (for all P phases)
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