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Remove extra overloads of muGas() and muWat().

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This change has been made in both BlackoilPropsAdInterface
and BlackoilPropsAdFromDeck. Only remaining overloads are
those using AD objects and passing the PhasePresence for
each data point.
This commit is contained in:
Atgeirr Flø Rasmussen
2015-03-03 13:14:31 +01:00
parent 965be0471f
commit 1d68f7e846
4 changed files with 9 additions and 192 deletions
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111
opm/autodiff/BlackoilPropsAdFromDeck.cpp
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@@ -312,85 +312,6 @@ BlackoilPropsAdFromDeck::BlackoilPropsAdFromDeck(const BlackoilPropsAdFromDeck&
// ------ Viscosity ------
/// Oil viscosity.
/// \param[in] po Array of n oil pressure values.
/// \param[in] T Array of n temperature values.
/// \param[in] rs Array of n gas solution factor values.
/// \param[in] cond Array of n taxonomies classifying fluid condition.
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
/// \return Array of n viscosity values.
V BlackoilPropsAdFromDeck::muOil(const V& po,
const V& T,
const V& rs,
const std::vector<PhasePresence>& cond,
const Cells& cells) const
{
if (!phase_usage_.phase_used[Oil]) {
OPM_THROW(std::runtime_error, "Cannot call muOil(): oil phase not present.");
}
const int n = cells.size();
mapPvtRegions(cells);
assert(po.size() == n);
V mu(n);
V dmudp(n);
V dmudr(n);
props_[phase_usage_.phase_pos[Oil]]->mu(n, pvt_region_.data(), po.data(), T.data(), rs.data(), &cond[0],
mu.data(), dmudp.data(), dmudr.data());
return mu;
}
/// Gas viscosity.
/// \param[in] pg Array of n gas pressure values.
/// \param[in] T Array of n temperature values.
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
/// \return Array of n viscosity values.
V BlackoilPropsAdFromDeck::muGas(const V& pg,
const V& T,
const Cells& cells) const
{
if (!phase_usage_.phase_used[Gas]) {
OPM_THROW(std::runtime_error, "Cannot call muGas(): gas phase not present.");
}
const int n = cells.size();
mapPvtRegions(cells);
assert(pg.size() == n);
V mu(n);
V dmudp(n);
V dmudr(n);
const double* rs = 0;
props_[phase_usage_.phase_pos[Gas]]->mu(n, pvt_region_.data(), pg.data(), T.data(), rs,
mu.data(), dmudp.data(), dmudr.data());
return mu;
}
/// Gas viscosity.
/// \param[in] pg Array of n gas pressure values.
/// \param[in] T Array of n temperature values.
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
/// \return Array of n viscosity values.
V BlackoilPropsAdFromDeck::muGas(const V& pg,
const V& T,
const V& rv,
const std::vector<PhasePresence>& cond,
const Cells& cells) const
{
if (!phase_usage_.phase_used[Gas]) {
OPM_THROW(std::runtime_error, "Cannot call muGas(): gas phase not present.");
}
const int n = cells.size();
mapPvtRegions(cells);
assert(pg.size() == n);
V mu(n);
V dmudp(n);
V dmudr(n);
props_[phase_usage_.phase_pos[Gas]]->mu(n, pvt_region_.data(), pg.data(), T.data(), rv.data(),&cond[0],
mu.data(), dmudp.data(), dmudr.data());
return mu;
}
/// Water viscosity.
/// \param[in] pw Array of n water pressure values.
/// \param[in] T Array of n temperature values.
@@ -465,38 +386,6 @@ BlackoilPropsAdFromDeck::BlackoilPropsAdFromDeck(const BlackoilPropsAdFromDeck&
return ADB::function(mu, jacs);
}
/// Gas viscosity.
/// \param[in] pg Array of n gas pressure values.
/// \param[in] T Array of n temperature values.
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
/// \return Array of n viscosity values.
ADB BlackoilPropsAdFromDeck::muGas(const ADB& pg,
const ADB& T,
const Cells& cells) const
{
if (!phase_usage_.phase_used[Gas]) {
OPM_THROW(std::runtime_error, "Cannot call muGas(): gas phase not present.");
}
const int n = cells.size();
mapPvtRegions(cells);
assert(pg.value().size() == n);
V mu(n);
V dmudp(n);
V dmudr(n);
const double* rv = 0;
props_[phase_usage_.phase_pos[Gas]]->mu(n, pvt_region_.data(), pg.value().data(), T.value().data(), rv,
mu.data(), dmudp.data(), dmudr.data());
ADB::M dmudp_diag = spdiag(dmudp);
const int num_blocks = pg.numBlocks();
std::vector<ADB::M> jacs(num_blocks);
for (int block = 0; block < num_blocks; ++block) {
fastSparseProduct(dmudp_diag, pg.derivative()[block], jacs[block]);
}
return ADB::function(mu, jacs);
}
/// Gas viscosity.
/// \param[in] pg Array of n gas pressure values.
/// \param[in] T Array of n temperature values.