diff --git a/dumux/material/constraintsolvers/compositionfromfugacities2pncmin.hh b/dumux/material/constraintsolvers/compositionfromfugacities2pncmin.hh
index 1596b9ef18fffa288b10f2f90a95992c6d9aa626..dcb295fcdcde07acd2d7f8740cee9adc2a3ca02d 100644
--- a/dumux/material/constraintsolvers/compositionfromfugacities2pncmin.hh
+++ b/dumux/material/constraintsolvers/compositionfromfugacities2pncmin.hh
@@ -144,8 +144,8 @@ protected:
};
template <class Scalar, class FluidSystem>
-DUNE_DEPRECATED_MSG("compositionFromFugacities2pncmin is deprecated. Use CompositionFromFugacities2pncmin (capital C) instead.")
-class compositionFromFugacities2pncmin
+class DUNE_DEPRECATED_MSG("compositionFromFugacities2pncmin is deprecated. Use CompositionFromFugacities2pncmin (capital C) instead.")
+ compositionFromFugacities2pncmin
: public CompositionFromFugacities2pncmin<Scalar, FluidSystem>
{ };
} // end namespace Dumux
diff --git a/dumux/porousmediumflow/2pnc/implicit/model.hh b/dumux/porousmediumflow/2pnc/implicit/model.hh
index b8bbeccb86d6fe456a91c8f588b488fc3488fa22..0f4a7446c84d203aa3c95f38d752e40ca1b51455 100644
--- a/dumux/porousmediumflow/2pnc/implicit/model.hh
+++ b/dumux/porousmediumflow/2pnc/implicit/model.hh
@@ -171,15 +171,15 @@ public:
// register standardized vtk output fields
auto& vtkOutputModule = problem.vtkOutputModule();
- vtkOutputModule.addSecondaryVariable("Sg", [](const VolumeVariables& v){ return v.saturation(nPhaseIdx); });
- vtkOutputModule.addSecondaryVariable("Sl", [](const VolumeVariables& v){ return v.saturation(wPhaseIdx); });
- vtkOutputModule.addSecondaryVariable("pg", [](const VolumeVariables& v){ return v.pressure(nPhaseIdx); });
- vtkOutputModule.addSecondaryVariable("pl", [](const VolumeVariables& v){ return v.pressure(wPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("Sn", [](const VolumeVariables& v){ return v.saturation(nPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("Sw", [](const VolumeVariables& v){ return v.saturation(wPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("pn", [](const VolumeVariables& v){ return v.pressure(nPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("pw", [](const VolumeVariables& v){ return v.pressure(wPhaseIdx); });
vtkOutputModule.addSecondaryVariable("pc", [](const VolumeVariables& v){ return v.capillaryPressure(); });
- vtkOutputModule.addSecondaryVariable("rhoL", [](const VolumeVariables& v){ return v.density(wPhaseIdx); });
- vtkOutputModule.addSecondaryVariable("rhoG", [](const VolumeVariables& v){ return v.density(nPhaseIdx); });
- vtkOutputModule.addSecondaryVariable("mobL", [](const VolumeVariables& v){ return v.mobility(wPhaseIdx); });
- vtkOutputModule.addSecondaryVariable("mobG", [](const VolumeVariables& v){ return v.mobility(nPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("rhoW", [](const VolumeVariables& v){ return v.density(wPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("rhoN", [](const VolumeVariables& v){ return v.density(nPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("mobW", [](const VolumeVariables& v){ return v.mobility(wPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("mobN", [](const VolumeVariables& v){ return v.mobility(nPhaseIdx); });
vtkOutputModule.addSecondaryVariable("porosity", [](const VolumeVariables& v){ return v.porosity(); });
vtkOutputModule.addSecondaryVariable("temperature", [](const VolumeVariables& v){ return v.temperature(); });
diff --git a/dumux/porousmediumflow/2pnc/implicit/propertydefaults.hh b/dumux/porousmediumflow/2pnc/implicit/propertydefaults.hh
index 7fb042c2639dc6f50a00ce3cf5ddafecbf0488ee..2947aa6477bcc1c11a4591717bbc645214fac9a1 100644
--- a/dumux/porousmediumflow/2pnc/implicit/propertydefaults.hh
+++ b/dumux/porousmediumflow/2pnc/implicit/propertydefaults.hh
@@ -74,7 +74,7 @@ private:
public:
static const int value = FluidSystem::numComponents;
};
-//! The major components belonging to the existing phases are mentioned here e.g., 2 for water and air being the major component in the liquid and gas phases in a 2 phase system
+//! The major components belonging to the existing phases, e.g. 2 for water and air being the major components in a liquid-gas-phase system
SET_PROP(TwoPNC, NumMajorComponents)
{
private:
@@ -83,7 +83,7 @@ private:
public:
static const int value = FluidSystem::numPhases;
static_assert(value == 2,
- "The model is restricted to two-phases, thus number of major components must also be two.");
+ "The model is restricted to two phases, thus number of major components must also be two.");
};
/*!
diff --git a/dumux/porousmediumflow/2pnc/implicit/volumevariables.hh b/dumux/porousmediumflow/2pnc/implicit/volumevariables.hh
index b67ec289dc9d18edc43309f16030a66ceb352feb..251a6345fb7309d46a5b84b47be9f8a8ec3715bb 100644
--- a/dumux/porousmediumflow/2pnc/implicit/volumevariables.hh
+++ b/dumux/porousmediumflow/2pnc/implicit/volumevariables.hh
@@ -138,7 +138,7 @@ public:
Scalar kr;
if (phaseIdx == wPhaseIdx)
kr = MaterialLaw::krw(materialParams, saturation(wPhaseIdx));
- else // ATTENTION: krn requires the liquid saturation // as parameter!
+ else // ATTENTION: krn requires the wetting-phase saturation as parameter!
kr = MaterialLaw::krn(materialParams, saturation(wPhaseIdx));
mobility_[phaseIdx] = kr / fluidState_.viscosity(phaseIdx);
@@ -252,7 +252,7 @@ public:
if (phasePresence == bothPhases)
{
// both phases are present, phase composition results from
- // the gas <-> liquid equilibrium. This is
+ // the nonwetting <-> wetting equilibrium. This is
// the job of the "MiscibleMultiPhaseComposition"
// constraint solver
@@ -279,12 +279,12 @@ public:
moleFrac[compIdx] = priVars[compIdx];
- Scalar sumMoleFracNotGas = 0;
+ Scalar sumMoleFracOtherComponents = 0;
for (int compIdx=numMajorComponents; compIdx<numComponents; ++compIdx)
- sumMoleFracNotGas+=moleFrac[compIdx];
+ sumMoleFracOtherComponents+=moleFrac[compIdx];
- sumMoleFracNotGas += moleFrac[wCompIdx];
- moleFrac[nCompIdx] = 1 - sumMoleFracNotGas;
+ sumMoleFracOtherComponents += moleFrac[wCompIdx];
+ moleFrac[nCompIdx] = 1 - sumMoleFracOtherComponents;
// Set fluid state mole fractions
@@ -303,9 +303,9 @@ public:
}
else if (phasePresence == wPhaseOnly){
- // only the liquid phase is present, i.e. liquid phase
+ // only the wetting phase is present, i.e. wetting phase
// composition is stored explicitly.
- // extract _mass_ fractions in the gas phase
+ // extract _mass_ fractions in the nonwetting phase
Dune::FieldVector<Scalar, numComponents> moleFrac;
for (int compIdx=numMajorComponents; compIdx<numComponents; ++compIdx)
diff --git a/dumux/porousmediumflow/2pncmin/implicit/model.hh b/dumux/porousmediumflow/2pncmin/implicit/model.hh
index 71ea2114749f213e0078bcf1a2e23197dd9fad1b..313167208f4d28fffd3b39d00cd34a13a3777d9b 100644
--- a/dumux/porousmediumflow/2pncmin/implicit/model.hh
+++ b/dumux/porousmediumflow/2pncmin/implicit/model.hh
@@ -157,15 +157,15 @@ public:
// register standardized vtk output fields
auto& vtkOutputModule = problem.vtkOutputModule();
- vtkOutputModule.addSecondaryVariable("Sg", [](const VolumeVariables& v){ return v.saturation(nPhaseIdx); });
- vtkOutputModule.addSecondaryVariable("Sl", [](const VolumeVariables& v){ return v.saturation(wPhaseIdx); });
- vtkOutputModule.addSecondaryVariable("pg", [](const VolumeVariables& v){ return v.pressure(nPhaseIdx); });
- vtkOutputModule.addSecondaryVariable("pl", [](const VolumeVariables& v){ return v.pressure(wPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("Sn", [](const VolumeVariables& v){ return v.saturation(nPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("Sw", [](const VolumeVariables& v){ return v.saturation(wPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("pn", [](const VolumeVariables& v){ return v.pressure(nPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("pw", [](const VolumeVariables& v){ return v.pressure(wPhaseIdx); });
vtkOutputModule.addSecondaryVariable("pc", [](const VolumeVariables& v){ return v.capillaryPressure(); });
- vtkOutputModule.addSecondaryVariable("rhoL", [](const VolumeVariables& v){ return v.density(wPhaseIdx); });
- vtkOutputModule.addSecondaryVariable("rhoG", [](const VolumeVariables& v){ return v.density(nPhaseIdx); });
- vtkOutputModule.addSecondaryVariable("mobL", [](const VolumeVariables& v){ return v.mobility(wPhaseIdx); });
- vtkOutputModule.addSecondaryVariable("mobG", [](const VolumeVariables& v){ return v.mobility(nPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("rhoW", [](const VolumeVariables& v){ return v.density(wPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("rhoN", [](const VolumeVariables& v){ return v.density(nPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("mobW", [](const VolumeVariables& v){ return v.mobility(wPhaseIdx); });
+ vtkOutputModule.addSecondaryVariable("mobN", [](const VolumeVariables& v){ return v.mobility(nPhaseIdx); });
vtkOutputModule.addSecondaryVariable("porosity", [](const VolumeVariables& v){ return v.porosity(); });
vtkOutputModule.addSecondaryVariable("temperature", [](const VolumeVariables& v){ return v.temperature(); });
diff --git a/dumux/porousmediumflow/2pncmin/implicit/volumevariables.hh b/dumux/porousmediumflow/2pncmin/implicit/volumevariables.hh
index d1eef18990ad9f7ad848416800306126ec429178..b8ac1cb2c17926ba25737fa6d5dc7110011448d7 100644
--- a/dumux/porousmediumflow/2pncmin/implicit/volumevariables.hh
+++ b/dumux/porousmediumflow/2pncmin/implicit/volumevariables.hh
@@ -247,7 +247,7 @@ public:
if (phasePresence == bothPhases)
{
// both phases are present, phase composition results from
- // the gas <-> liquid equilibrium. This is
+ // the nonwetting <-> wetting equilibrium. This is
// the job of the "MiscibleMultiPhaseComposition"
// constraint solver
@@ -286,12 +286,12 @@ public:
/(fugCoeffG[compIdx]*fluidState.pressure(nPhaseIdx));
moleFrac[wCompIdx] = priVars[switchIdx];
- Scalar sumMoleFracNotGas = 0;
+ Scalar sumMoleFracOtherComponents = 0;
for (int compIdx=numMajorComponents; compIdx<numComponents; ++compIdx)
- sumMoleFracNotGas+=moleFrac[compIdx];
+ sumMoleFracOtherComponents+=moleFrac[compIdx];
- sumMoleFracNotGas += moleFrac[wCompIdx];
- moleFrac[nCompIdx] = 1 - sumMoleFracNotGas;
+ sumMoleFracOtherComponents += moleFrac[wCompIdx];
+ moleFrac[nCompIdx] = 1 - sumMoleFracOtherComponents;
// Set fluid state mole fractions
for (int compIdx=0; compIdx<numComponents; ++compIdx)
@@ -312,9 +312,9 @@ public:
}
else if (phasePresence == wPhaseOnly)
{
- // only the liquid phase is present, i.e. liquid phase
+ // only the wetting phase is present, i.e. wetting
// composition is stored explicitly.
- // extract _mass_ fractions in the gas phase
+ // extract _mass_ fractions in the nonwetting phase
Dune::FieldVector<Scalar, numComponents> moleFrac;
for (int compIdx=numMajorComponents; compIdx<numComponents; ++compIdx)
@@ -375,7 +375,7 @@ public:
// { return initialPorosity_;}
// /*!
- // * \brief Returns the mole fraction of the salinity in the liquid phase
+ // * \brief Returns the mole fraction of the salinity in the wetting phase
// */
// Scalar moleFracSalinity() const
// {
@@ -383,7 +383,7 @@ public:
// }
// /*!
- // * \brief Returns the salinity (mass fraction) in the liquid phase
+ // * \brief Returns the salinity (mass fraction) in the wetting phase
// */
// Scalar salinity() const
// {
diff --git a/test/references/fuelcell2pncbox-reference.vtu b/test/references/fuelcell2pncbox-reference.vtu
index 80abd5597f0a53e04d8b3ba3d256a80b15c63be5..51349dfa14bf560ec3dcdf083b9860edafb5c54e 100644
--- a/test/references/fuelcell2pncbox-reference.vtu
+++ b/test/references/fuelcell2pncbox-reference.vtu
@@ -2,8 +2,8 @@
<VTKFile type="UnstructuredGrid" version="0.1" byte_order="LittleEndian">
<UnstructuredGrid>
<Piece NumberOfCells="126" NumberOfPoints="154">
- <PointData Scalars="Sg">
- <DataArray type="Float32" Name="Sg" NumberOfComponents="1" format="ascii">
+ <PointData Scalars="Sn">
+ <DataArray type="Float32" Name="Sn" NumberOfComponents="1" format="ascii">
0.699989 0.699989 0.699991 0.699991 0.699989 0.699991 0.699989 0.699991 0.699989 0.699991 0.699989 0.699991
0.699989 0.699991 0.699989 0.699991 0.699989 0.699991 0.699989 0.699991 0.699989 0.699991 0.699989 0.699991
0.699989 0.699991 0.699989 0.699991 0.699989 0.699991 0.699989 0.699991 0.699989 0.699991 0.699989 0.699991
@@ -18,7 +18,7 @@
0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7
0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7
</DataArray>
- <DataArray type="Float32" Name="Sl" NumberOfComponents="1" format="ascii">
+ <DataArray type="Float32" Name="Sw" NumberOfComponents="1" format="ascii">
0.300011 0.300011 0.300009 0.300009 0.300011 0.300009 0.300011 0.300009 0.300011 0.300009 0.300011 0.300009
0.300011 0.300009 0.300011 0.300009 0.300011 0.300009 0.300011 0.300009 0.300011 0.300009 0.300011 0.300009
0.300011 0.300009 0.300011 0.300009 0.300011 0.300009 0.300011 0.300009 0.300011 0.300009 0.300011 0.300009
@@ -33,7 +33,7 @@
0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3
0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3
</DataArray>
- <DataArray type="Float32" Name="pg" NumberOfComponents="1" format="ascii">
+ <DataArray type="Float32" Name="pn" NumberOfComponents="1" format="ascii">
99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8
99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8
99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8 99999.8
@@ -48,7 +48,7 @@
100000 100000 100000 100000 100000 100000 100000 100000 100000 100000 100000 100000
100000 100000 100000 100000 100000 100000 100000 100000 100000 100000
</DataArray>
- <DataArray type="Float32" Name="pl" NumberOfComponents="1" format="ascii">
+ <DataArray type="Float32" Name="pw" NumberOfComponents="1" format="ascii">
111440 111440 111440 111440 111440 111440 111440 111440 111440 111440 111440 111440
111440 111440 111440 111440 111440 111440 111440 111440 111440 111440 111440 111440
111440 111440 111440 111440 111440 111440 111440 111440 111440 111440 111440 111440
@@ -78,7 +78,7 @@
-11440.1 -11440.1 -11440.1 -11440.1 -11440.1 -11440.1 -11440.1 -11440.1 -11440.1 -11440.1 -11440.1 -11440.1
-11440.1 -11440.1 -11440.1 -11440.1 -11440.1 -11440.1 -11440.1 -11440.1 -11440.1 -11440.1
</DataArray>
- <DataArray type="Float32" Name="rhoL" NumberOfComponents="1" format="ascii">
+ <DataArray type="Float32" Name="rhoW" NumberOfComponents="1" format="ascii">
993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402
993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402
993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402 993.402
@@ -93,7 +93,7 @@
993.403 993.403 993.403 993.403 993.403 993.403 993.403 993.403 993.403 993.403 993.403 993.403
993.403 993.403 993.403 993.403 993.403 993.403 993.403 993.403 993.403 993.403
</DataArray>
- <DataArray type="Float32" Name="rhoG" NumberOfComponents="1" format="ascii">
+ <DataArray type="Float32" Name="rhoN" NumberOfComponents="1" format="ascii">
1.0976 1.0976 1.10151 1.10151 1.0976 1.10151 1.0976 1.10151 1.0976 1.10151 1.0976 1.10151
1.0976 1.10151 1.0976 1.10151 1.0976 1.10151 1.0976 1.10151 1.0976 1.10151 1.0976 1.10151
1.0976 1.10151 1.0976 1.10151 1.0976 1.10151 1.0976 1.10151 1.0976 1.10151 1.0976 1.10151
@@ -108,7 +108,7 @@
1.11907 1.11907 1.11907 1.11907 1.11907 1.11907 1.11907 1.11907 1.11907 1.11907 1.11907 1.11907
1.11907 1.11907 1.11907 1.11907 1.11907 1.11907 1.11907 1.11907 1.11907 1.11907
</DataArray>
- <DataArray type="Float32" Name="mobL" NumberOfComponents="1" format="ascii">
+ <DataArray type="Float32" Name="mobW" NumberOfComponents="1" format="ascii">
129.817 129.817 129.816 129.816 129.817 129.816 129.817 129.816 129.817 129.816 129.817 129.816
129.817 129.816 129.817 129.816 129.817 129.816 129.817 129.816 129.817 129.816 129.817 129.816
129.817 129.816 129.817 129.816 129.817 129.816 129.817 129.816 129.817 129.816 129.817 129.816
@@ -123,7 +123,7 @@
129.808 129.808 129.808 129.808 129.808 129.808 129.808 129.808 129.808 129.808 129.808 129.808
129.808 129.808 129.808 129.808 129.808 129.808 129.808 129.808 129.808 129.808
</DataArray>
- <DataArray type="Float32" Name="mobG" NumberOfComponents="1" format="ascii">
+ <DataArray type="Float32" Name="mobN" NumberOfComponents="1" format="ascii">
18761 18761 18685.6 18685.6 18761 18685.6 18761 18685.6 18761 18685.6 18761 18685.6
18761 18685.6 18761 18685.6 18761 18685.6 18761 18685.6 18761 18685.6 18761 18685.6
18761 18685.6 18761 18685.6 18761 18685.6 18761 18685.6 18761 18685.6 18761 18685.6
@@ -168,51 +168,6 @@
310 310 310 310 310 310 310 310 310 310 310 310
310 310 310 310 310 310 310 310 310 310
</DataArray>
- <DataArray type="Float32" Name="reactionSourceH2O [mol/(sm^2)]" NumberOfComponents="1" format="ascii">
- 747.822 747.822 0 0 747.822 0 747.822 0 747.822 0 747.822 0
- 747.822 0 747.822 0 747.822 0 747.822 0 747.822 0 747.822 0
- 747.822 0 747.822 0 747.822 0 747.822 0 747.822 0 747.822 0
- 747.822 0 747.822 0 747.822 0 747.822 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0
- </DataArray>
- <DataArray type="Float32" Name="reactionSourceO2 [mol/(sm^2)]" NumberOfComponents="1" format="ascii">
- -255.16 -255.16 0 0 -255.16 0 -255.16 0 -255.16 0 -255.16 0
- -255.16 0 -255.16 0 -255.16 0 -255.16 0 -255.16 0 -255.16 0
- -255.16 0 -255.16 0 -255.16 0 -255.16 0 -255.16 0 -255.16 0
- -255.16 0 -255.16 0 -255.16 0 -255.16 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0
- </DataArray>
- <DataArray type="Float32" Name="currentDensity [A/cm^2]" NumberOfComponents="1" format="ascii">
- 0.451352 0.451352 0 0 0.451352 0 0.451352 0 0.451352 0 0.451352 0
- 0.451352 0 0.451352 0 0.451352 0 0.451352 0 0.451352 0 0.451352 0
- 0.451352 0 0.451352 0 0.451352 0 0.451352 0 0.451352 0 0.451352 0
- 0.451352 0 0.451352 0 0.451352 0 0.451352 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0 0 0
- 0 0 0 0 0 0 0 0 0 0
- </DataArray>
<DataArray type="Float32" Name="Kxx" NumberOfComponents="1" format="ascii">
5e-11 5e-11 5e-11 5e-11 5e-11 5e-11 5e-11 5e-11 5e-11 5e-11 5e-11 5e-11
5e-11 5e-11 5e-11 5e-11 5e-11 5e-11 5e-11 5e-11 5e-11 5e-11 5e-11 5e-11
@@ -378,6 +333,51 @@
0.383375 0.383375 0.383375 0.383375 0.383375 0.383375 0.383375 0.383375 0.383375 0.383375 0.383375 0.383375
0.383375 0.383375 0.383375 0.383375 0.383375 0.383375 0.383375 0.383375 0.383375 0.383375
</DataArray>
+ <DataArray type="Float32" Name="reactionSourceH2O [mol/(sm^2)]" NumberOfComponents="1" format="ascii">
+ 747.822 747.822 0 0 747.822 0 747.822 0 747.822 0 747.822 0
+ 747.822 0 747.822 0 747.822 0 747.822 0 747.822 0 747.822 0
+ 747.822 0 747.822 0 747.822 0 747.822 0 747.822 0 747.822 0
+ 747.822 0 747.822 0 747.822 0 747.822 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0
+ </DataArray>
+ <DataArray type="Float32" Name="reactionSourceO2 [mol/(sm^2)]" NumberOfComponents="1" format="ascii">
+ -255.16 -255.16 0 0 -255.16 0 -255.16 0 -255.16 0 -255.16 0
+ -255.16 0 -255.16 0 -255.16 0 -255.16 0 -255.16 0 -255.16 0
+ -255.16 0 -255.16 0 -255.16 0 -255.16 0 -255.16 0 -255.16 0
+ -255.16 0 -255.16 0 -255.16 0 -255.16 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0 0 0
+ 0 0 0 0 0 0 0 0 0 0
+ </DataArray>
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diff --git a/test/references/fuelcell2pnccc-reference.vtu b/test/references/fuelcell2pnccc-reference.vtu
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--- a/test/references/fuelcell2pnccc-reference.vtu
+++ b/test/references/fuelcell2pnccc-reference.vtu
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diff --git a/test/references/saltflushbox2pncmin-reference.vtu b/test/references/saltflushbox2pncmin-reference.vtu
index 8d1ce3d9e2261db49764c0afdc773d378c614301..e2b9e4b3f36f3822987654e497b5af9a59e55bc3 100644
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+++ b/test/references/saltflushbox2pncmin-reference.vtu
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diff --git a/test/references/saltflushcc2pncmin-reference.vtu b/test/references/saltflushcc2pncmin-reference.vtu
index ebf73404aedb65bcec08c218a5b5d3dd6f717f80..68c61c057b35af984a667f3cfef244811c58af95 100644
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