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rename some variables from "*Lad" to "*Eval"

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this was an involuntary omission in the "local AD" to "dense AD"
rename...
This commit is contained in:
Andreas Lauser 2016-06-06 14:33:54 +02:00
parent 807261b084
commit 8a6243962d
1 changed files with 94 additions and 94 deletions
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188
opm/core/props/BlackoilPropertiesFromDeck.cpp
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@ -244,15 +244,15 @@ namespace Opm
const auto& pu = phaseUsage();
const int np = numPhases();
typedef Opm::DenseAd::Evaluation<double, /*size=*/1> LadEval;
typedef Opm::DenseAd::Evaluation<double, /*size=*/1> Eval;
LadEval pLad = 0.0;
LadEval TLad = 0.0;
LadEval RsLad = 0.0;
LadEval RvLad = 0.0;
LadEval muLad = 0.0;
Eval pEval = 0.0;
Eval TEval = 0.0;
Eval RsEval = 0.0;
Eval RvEval = 0.0;
Eval muEval = 0.0;
pLad.derivatives[0] = 1.0;
pEval.derivatives[0] = 1.0;
R_.resize(n*np);
this->compute_R_(n, p, T, z, cells, &R_[0]);
@ -260,30 +260,30 @@ namespace Opm
for (int i = 0; i < n; ++ i) {
int cellIdx = cells[i];
int pvtRegionIdx = cellPvtRegionIdx_[cellIdx];
pLad.value = p[i];
TLad.value = T[i];
pEval.value = p[i];
TEval.value = T[i];
if (pu.phase_used[BlackoilPhases::Aqua]) {
muLad = waterPvt_.viscosity(pvtRegionIdx, TLad, pLad);
muEval = waterPvt_.viscosity(pvtRegionIdx, TEval, pEval);
int offset = pu.num_phases*cellIdx + pu.phase_pos[BlackoilPhases::Aqua];
mu[offset] = muLad.value;
dmudp[offset] = muLad.derivatives[0];
mu[offset] = muEval.value;
dmudp[offset] = muEval.derivatives[0];
}
if (pu.phase_used[BlackoilPhases::Liquid]) {
RsLad.value = R_[i*np + pu.phase_pos[BlackoilPhases::Liquid]];
muLad = oilPvt_.viscosity(pvtRegionIdx, TLad, pLad, RsLad);
RsEval.value = R_[i*np + pu.phase_pos[BlackoilPhases::Liquid]];
muEval = oilPvt_.viscosity(pvtRegionIdx, TEval, pEval, RsEval);
int offset = pu.num_phases*cellIdx + pu.phase_pos[BlackoilPhases::Liquid];
mu[offset] = muLad.value;
dmudp[offset] = muLad.derivatives[0];
mu[offset] = muEval.value;
dmudp[offset] = muEval.derivatives[0];
}
if (pu.phase_used[BlackoilPhases::Vapour]) {
RvLad.value = R_[i*np + pu.phase_pos[BlackoilPhases::Vapour]];
muLad = gasPvt_.viscosity(pvtRegionIdx, TLad, pLad, RvLad);
RvEval.value = R_[i*np + pu.phase_pos[BlackoilPhases::Vapour]];
muEval = gasPvt_.viscosity(pvtRegionIdx, TEval, pEval, RvEval);
int offset = pu.num_phases*cellIdx + pu.phase_pos[BlackoilPhases::Vapour];
mu[offset] = muLad.value;
dmudp[offset] = muLad.derivatives[0];
mu[offset] = muEval.value;
dmudp[offset] = muEval.derivatives[0];
}
}
}
@ -396,27 +396,27 @@ namespace Opm
{
const auto& pu = phaseUsage();
typedef double LadEval;
typedef double Eval;
LadEval pLad = 0.0;
LadEval TLad = 0.0;
LadEval RsLad = 0.0;
LadEval RvLad = 0.0;
Eval pEval = 0.0;
Eval TEval = 0.0;
Eval RsEval = 0.0;
Eval RvEval = 0.0;
for (int i = 0; i < n; ++ i) {
int cellIdx = cells[i];
int pvtRegionIdx = cellPvtRegionIdx_[cellIdx];
pLad = p[i];
TLad = T[i];
pEval = p[i];
TEval = T[i];
int oilOffset = pu.num_phases*i + pu.phase_pos[BlackoilPhases::Liquid];
int gasOffset = pu.num_phases*i + pu.phase_pos[BlackoilPhases::Vapour];
int waterOffset = pu.num_phases*i + pu.phase_pos[BlackoilPhases::Aqua];
if (pu.phase_used[BlackoilPhases::Aqua]) {
LadEval BLad = 1.0/waterPvt_.inverseFormationVolumeFactor(pvtRegionIdx, TLad, pLad);
Eval BEval = 1.0/waterPvt_.inverseFormationVolumeFactor(pvtRegionIdx, TEval, pEval);
B[waterOffset] = BLad;
B[waterOffset] = BEval;
}
if (pu.phase_used[BlackoilPhases::Liquid]) {
@ -424,18 +424,18 @@ namespace Opm
double maxRs = 0.0;
if (pu.phase_used[BlackoilPhases::Vapour]) {
currentRs = (z[oilOffset] == 0.0) ? 0.0 : z[gasOffset]/z[oilOffset];
maxRs = oilPvt_.saturatedGasDissolutionFactor(pvtRegionIdx, TLad, pLad);
maxRs = oilPvt_.saturatedGasDissolutionFactor(pvtRegionIdx, TEval, pEval);
}
LadEval BLad;
Eval BEval;
if (currentRs >= maxRs) {
BLad = 1.0/oilPvt_.saturatedInverseFormationVolumeFactor(pvtRegionIdx, TLad, pLad);
BEval = 1.0/oilPvt_.saturatedInverseFormationVolumeFactor(pvtRegionIdx, TEval, pEval);
}
else {
RsLad = currentRs;
BLad = 1.0/oilPvt_.inverseFormationVolumeFactor(pvtRegionIdx, TLad, pLad, RsLad);
RsEval = currentRs;
BEval = 1.0/oilPvt_.inverseFormationVolumeFactor(pvtRegionIdx, TEval, pEval, RsEval);
}
B[oilOffset] = BLad;
B[oilOffset] = BEval;
}
if (pu.phase_used[BlackoilPhases::Vapour]) {
@ -443,18 +443,18 @@ namespace Opm
double maxRv = 0.0;
if (pu.phase_used[BlackoilPhases::Liquid]) {
currentRv = (z[gasOffset] == 0.0) ? 0.0 : z[oilOffset]/z[gasOffset];
maxRv = gasPvt_.saturatedOilVaporizationFactor(pvtRegionIdx, TLad, pLad);
maxRv = gasPvt_.saturatedOilVaporizationFactor(pvtRegionIdx, TEval, pEval);
}
LadEval BLad;
Eval BEval;
if (currentRv >= maxRv) {
BLad = 1.0/gasPvt_.saturatedInverseFormationVolumeFactor(pvtRegionIdx, TLad, pLad);
BEval = 1.0/gasPvt_.saturatedInverseFormationVolumeFactor(pvtRegionIdx, TEval, pEval);
}
else {
RvLad = currentRv;
BLad = 1.0/gasPvt_.inverseFormationVolumeFactor(pvtRegionIdx, TLad, pLad, RvLad);
RvEval = currentRv;
BEval = 1.0/gasPvt_.inverseFormationVolumeFactor(pvtRegionIdx, TEval, pEval, RvEval);
}
B[gasOffset] = BLad;
B[gasOffset] = BEval;
}
}
}
@ -469,30 +469,30 @@ namespace Opm
{
const auto& pu = phaseUsage();
typedef Opm::DenseAd::Evaluation<double, /*size=*/1> LadEval;
typedef Opm::DenseAd::Evaluation<double, /*size=*/1> Eval;
LadEval pLad = 0.0;
LadEval TLad = 0.0;
LadEval RsLad = 0.0;
LadEval RvLad = 0.0;
Eval pEval = 0.0;
Eval TEval = 0.0;
Eval RsEval = 0.0;
Eval RvEval = 0.0;
pLad.derivatives[0] = 1.0;
pEval.derivatives[0] = 1.0;
for (int i = 0; i < n; ++ i) {
int cellIdx = cells[i];
int pvtRegionIdx = cellPvtRegionIdx_[cellIdx];
pLad.value = p[i];
TLad.value = T[i];
pEval.value = p[i];
TEval.value = T[i];
int oilOffset = pu.num_phases*i + pu.phase_pos[BlackoilPhases::Liquid];
int gasOffset = pu.num_phases*i + pu.phase_pos[BlackoilPhases::Vapour];
int waterOffset = pu.num_phases*i + pu.phase_pos[BlackoilPhases::Aqua];
if (pu.phase_used[BlackoilPhases::Aqua]) {
LadEval BLad = 1.0/waterPvt_.inverseFormationVolumeFactor(pvtRegionIdx, TLad, pLad);
Eval BEval = 1.0/waterPvt_.inverseFormationVolumeFactor(pvtRegionIdx, TEval, pEval);
B[waterOffset] = BLad.value;
dBdp[waterOffset] = BLad.derivatives[0];
B[waterOffset] = BEval.value;
dBdp[waterOffset] = BEval.derivatives[0];
}
if (pu.phase_used[BlackoilPhases::Liquid]) {
@ -500,19 +500,19 @@ namespace Opm
double maxRs = 0.0;
if (pu.phase_used[BlackoilPhases::Vapour]) {
currentRs = (z[oilOffset] == 0.0) ? 0.0 : z[gasOffset]/z[oilOffset];
maxRs = oilPvt_.saturatedGasDissolutionFactor(pvtRegionIdx, TLad.value, pLad.value);
maxRs = oilPvt_.saturatedGasDissolutionFactor(pvtRegionIdx, TEval.value, pEval.value);
}
LadEval BLad;
Eval BEval;
if (currentRs >= maxRs) {
BLad = 1.0/oilPvt_.saturatedInverseFormationVolumeFactor(pvtRegionIdx, TLad, pLad);
BEval = 1.0/oilPvt_.saturatedInverseFormationVolumeFactor(pvtRegionIdx, TEval, pEval);
}
else {
RsLad.value = currentRs;
BLad = 1.0/oilPvt_.inverseFormationVolumeFactor(pvtRegionIdx, TLad, pLad, RsLad);
RsEval.value = currentRs;
BEval = 1.0/oilPvt_.inverseFormationVolumeFactor(pvtRegionIdx, TEval, pEval, RsEval);
}
B[oilOffset] = BLad.value;
dBdp[oilOffset] = BLad.derivatives[0];
B[oilOffset] = BEval.value;
dBdp[oilOffset] = BEval.derivatives[0];
}
if (pu.phase_used[BlackoilPhases::Vapour]) {
@ -520,19 +520,19 @@ namespace Opm
double maxRv = 0.0;
if (pu.phase_used[BlackoilPhases::Liquid]) {
currentRv = (z[gasOffset] == 0.0) ? 0.0 : z[oilOffset]/z[gasOffset];
maxRv = gasPvt_.saturatedOilVaporizationFactor(pvtRegionIdx, TLad.value, pLad.value);
maxRv = gasPvt_.saturatedOilVaporizationFactor(pvtRegionIdx, TEval.value, pEval.value);
}
LadEval BLad;
Eval BEval;
if (currentRv >= maxRv) {
BLad = 1.0/gasPvt_.saturatedInverseFormationVolumeFactor(pvtRegionIdx, TLad, pLad);
BEval = 1.0/gasPvt_.saturatedInverseFormationVolumeFactor(pvtRegionIdx, TEval, pEval);
}
else {
RvLad.value = currentRv;
BLad = 1.0/gasPvt_.inverseFormationVolumeFactor(pvtRegionIdx, TLad, pLad, RvLad);
RvEval.value = currentRv;
BEval = 1.0/gasPvt_.inverseFormationVolumeFactor(pvtRegionIdx, TEval, pEval, RvEval);
}
B[gasOffset] = BLad.value;
dBdp[gasOffset] = BLad.derivatives[0];
B[gasOffset] = BEval.value;
dBdp[gasOffset] = BEval.derivatives[0];
}
}
}
@ -546,16 +546,16 @@ namespace Opm
{
const auto& pu = phaseUsage();
typedef double LadEval;
typedef double Eval;
LadEval pLad = 0.0;
LadEval TLad = 0.0;
Eval pEval = 0.0;
Eval TEval = 0.0;
for (int i = 0; i < n; ++ i) {
int cellIdx = cells[i];
int pvtRegionIdx = cellPvtRegionIdx_[cellIdx];
pLad = p[i];
TLad = T[i];
pEval = p[i];
TEval = T[i];
int oilOffset = pu.num_phases*i + pu.phase_pos[BlackoilPhases::Liquid];
int gasOffset = pu.num_phases*i + pu.phase_pos[BlackoilPhases::Vapour];
@ -566,29 +566,29 @@ namespace Opm
}
if (pu.phase_used[BlackoilPhases::Liquid]) {
LadEval RsSatLad = oilPvt_.saturatedGasDissolutionFactor(pvtRegionIdx, TLad, pLad);
Eval RsSatEval = oilPvt_.saturatedGasDissolutionFactor(pvtRegionIdx, TEval, pEval);
double currentRs = 0.0;
if (pu.phase_used[BlackoilPhases::Vapour]) {
currentRs = (z[oilOffset] == 0.0) ? 0.0 : z[gasOffset]/z[oilOffset];
}
RsSatLad = std::min(RsSatLad, currentRs);
RsSatEval = std::min(RsSatEval, currentRs);
R[oilOffset] = RsSatLad;
R[oilOffset] = RsSatEval;
}
if (pu.phase_used[BlackoilPhases::Vapour]) {
LadEval RvSatLad = gasPvt_.saturatedOilVaporizationFactor(pvtRegionIdx, TLad, pLad);
Eval RvSatEval = gasPvt_.saturatedOilVaporizationFactor(pvtRegionIdx, TEval, pEval);
double currentRv = 0.0;
if (pu.phase_used[BlackoilPhases::Liquid]) {
currentRv = (z[gasOffset] == 0.0) ? 0.0 : z[oilOffset]/z[gasOffset];
}
RvSatLad = std::min(RvSatLad, currentRv);
RvSatEval = std::min(RvSatEval, currentRv);
R[gasOffset] = RvSatLad;
R[gasOffset] = RvSatEval;
}
}
}
@ -603,19 +603,19 @@ namespace Opm
{
const auto& pu = phaseUsage();
typedef Opm::DenseAd::Evaluation<double, /*size=*/1> LadEval;
typedef Opm::MathToolbox<LadEval> Toolbox;
typedef Opm::DenseAd::Evaluation<double, /*size=*/1> Eval;
typedef Opm::MathToolbox<Eval> Toolbox;
LadEval pLad = 0.0;
LadEval TLad = 0.0;
Eval pEval = 0.0;
Eval TEval = 0.0;
pLad.derivatives[0] = 1.0;
pEval.derivatives[0] = 1.0;
for (int i = 0; i < n; ++ i) {
int cellIdx = cells[i];
int pvtRegionIdx = cellPvtRegionIdx_[cellIdx];
pLad.value = p[i];
TLad.value = T[i];
pEval.value = p[i];
TEval.value = T[i];
int oilOffset = pu.num_phases*i + pu.phase_pos[BlackoilPhases::Liquid];
int gasOffset = pu.num_phases*i + pu.phase_pos[BlackoilPhases::Vapour];
@ -626,31 +626,31 @@ namespace Opm
}
if (pu.phase_used[BlackoilPhases::Liquid]) {
LadEval RsSatLad = oilPvt_.saturatedGasDissolutionFactor(pvtRegionIdx, TLad, pLad);
Eval RsSatEval = oilPvt_.saturatedGasDissolutionFactor(pvtRegionIdx, TEval, pEval);
LadEval currentRs = 0.0;
Eval currentRs = 0.0;
if (pu.phase_used[BlackoilPhases::Vapour]) {
currentRs = (z[oilOffset] == 0.0) ? 0.0 : z[gasOffset]/z[oilOffset];
}
RsSatLad = Toolbox::min(RsSatLad, currentRs);
RsSatEval = Toolbox::min(RsSatEval, currentRs);
R[oilOffset] = RsSatLad.value;
dRdp[oilOffset] = RsSatLad.derivatives[0];
R[oilOffset] = RsSatEval.value;
dRdp[oilOffset] = RsSatEval.derivatives[0];
}
if (pu.phase_used[BlackoilPhases::Vapour]) {
LadEval RvSatLad = gasPvt_.saturatedOilVaporizationFactor(pvtRegionIdx, TLad, pLad);
Eval RvSatEval = gasPvt_.saturatedOilVaporizationFactor(pvtRegionIdx, TEval, pEval);
LadEval currentRv = 0.0;
Eval currentRv = 0.0;
if (pu.phase_used[BlackoilPhases::Liquid]) {
currentRv = (z[gasOffset] == 0.0) ? 0.0 : z[oilOffset]/z[gasOffset];
}
RvSatLad = Toolbox::min(RvSatLad, currentRv);
RvSatEval = Toolbox::min(RvSatEval, currentRv);
R[gasOffset] = RvSatLad.value;
dRdp[gasOffset] = RvSatLad.derivatives[0];
R[gasOffset] = RvSatEval.value;
dRdp[gasOffset] = RvSatEval.derivatives[0];
}
}
}