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Commit 0ccde397 authored by Gabi Seitz's avatar Gabi Seitz Committed by Timo Koch
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[vapor][fluidsystems] add method gasViscosityForMixtures 

with contributions of Holger and Bernd

The following test results had to be adapted:
test_md_boundary_darcy2p2c_stokes1p2c_horizontal
test_md_boundary_darcy2p2cni_stokes1p2cni_horizontal
test_2p1cni_steaminjection_waterwet_box
test_2p1cni_steaminjection_waterwet_tpfa
test_2p2cni_waterair_box
test_2p2cni_waterair_buoyancy_box
test_dec2p2c
test_multiphysics2p2c
test_1pncmin_box
test_3p3cni_kuevette_box
test_3p3cni_kuevette_tpfa
test_3pwateroil_sagd_box
parent ac3b2fa4
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Inline Side-by-side
dumux/material/components/h2o.hh
View file @ 0ccde397
......@@ -708,12 +708,14 @@ public:
* \param temperature temperature of component in \f$\mathrm{[K]}\f$
* \param pressure pressure of component in \f$\mathrm{[Pa]}\f$
*
* This method is only valid if pressure is below or at the vapor
* pressure of water.
* We assume pure water vapor here. For water in a mixture of other gaseous
* components, consider the free function h2oGasViscosityInMixture.
*
* See:
* We use the IAPWS Formulation, see:
* IAPWS: "Release on the IAPWS Formulation 2008 for the Viscosity
* of Ordinary Water Substance", http://www.iapws.org/relguide/visc.pdf \cite cooper2008
* This method is only valid if pressure is below or at the vapor
* pressure of water.
*/
static Scalar gasViscosity(Scalar temperature, Scalar pressure)
{
......@@ -723,6 +725,7 @@ public:
return Common::viscosity(temperature, rho);
}
/*!
* \brief The dynamic viscosity \f$\mathrm{[Pa*s]}\f$ of pure water.
*
......@@ -905,13 +908,88 @@ private:
Region2::dGamma_dPi(temperature, pressure) *
Rs * temperature / pressure;
}
}; // end class
};
template <class Scalar>
struct IsAqueous<H2O<Scalar>> : public std::true_type {};
} // end namespace Components
namespace FluidSystems::Detail {
// viscosity according to Reid, R.C.
template <class Scalar>
Scalar viscosityReid_(Scalar temperature)
{
constexpr Scalar tc = 647.3;
using std::max;
const Scalar tr = max(temperature/tc, 1e-8);
const Scalar fp0 = 1.0 + 0.221*(0.96 + 0.1*(tr - 0.7));
constexpr Scalar xi = 3.334e-3;
using std::pow;
using std::exp;
const Scalar eta_xi = (0.807*pow(tr, 0.618) - 0.357*exp((-0.449)*tr)
+ 0.34*exp((-4.058)*tr) + 0.018)*fp0;
return 1.0e-7*eta_xi/xi;
}
// viscosity according to Nagel, T. et al.
template <class Scalar>
Scalar viscosityNagel_(Scalar temperature)
{
constexpr Scalar a1 = -4.4189440e-6;
constexpr Scalar a2 = 4.6876380e-8;
constexpr Scalar a3 = -5.3894310e-12;
constexpr Scalar a4 = 3.2028560e-16;
constexpr Scalar a5 = 4.9191790e-22;
return a1 + a2*temperature + a3*temperature*temperature
+ a4*temperature*temperature*temperature
+ a5*temperature*temperature*temperature*temperature;
}
} // end FluidSystems::Detail
namespace FluidSystems {
/*!
* \brief The dynamic viscosity \f$\mathrm{[Pa*s]}\f$ of steam in a gas mixture.
*
* \param temperature temperature in \f$\mathrm{[K]}\f$
*
* We assume here that water is in mixture with other gaseous components.
* For pure water, use the gasViscosity function of Components::H2O.
*
* We apply two different laws depending on the gas temperature.
*
* For temperatures below 480 K see:
* "Reid, R.C., Prausnitz, J.M., Poling, B.E.: The Properties of
* Gases and Liquids (1987)"
* Lucas corresponding states method
* https://www.osti.gov/scitech/biblio/6504847} \cite{reid1987}
*
* For temperatures above 500 K see:
* Nagel, T. et al.: THC-Processes (2018)
* https://doi.org/10.1007/978-3-319-68225-9_12
*
* In the range 480 - 500 K, we interpolate between the two laws.
*/
template <class Scalar>
Scalar h2oGasViscosityInMixture(Scalar temperature, Scalar pressure)
{
if (temperature < 480.0)
return Detail::viscosityReid_(temperature);
else if (temperature > 500.0)
return Detail::viscosityNagel_(temperature);
else // interpolate
{
const Scalar op = (500.0 - temperature)/20.0;
return op*Detail::viscosityReid_(temperature)
+ (1.0 - op)*Detail::viscosityNagel_(temperature);
}
}
} // end namespace FluidSystems
} // end namespace Dumux
#endif
dumux/material/fluidsystems/h2oair.hh
View file @ 0ccde397
......@@ -481,8 +481,7 @@ public:
// Wilke method (Reid et al.):
Scalar muResult = 0;
const Scalar mu[numComponents] = {
H2O::gasViscosity(T,
H2O::vaporPressure(T)),
h2oGasViscosityInMixture(T, p),
Air::gasViscosity(T, p)
};
......
dumux/material/fluidsystems/h2oairmesitylene.hh
View file @ 0ccde397
......@@ -349,7 +349,7 @@ public:
*/
Scalar muResult;
const Scalar mu[numComponents] = {
H2O::gasViscosity(fluidState.temperature(phaseIdx), H2O::vaporPressure(fluidState.temperature(phaseIdx))),
h2oGasViscosityInMixture(fluidState.temperature(phaseIdx), fluidState.pressure(phaseIdx)),
Air::gasViscosity(fluidState.temperature(phaseIdx), fluidState.pressure(phaseIdx)),
NAPL::gasViscosity(fluidState.temperature(phaseIdx), NAPL::vaporPressure(fluidState.temperature(phaseIdx)))
};
......
dumux/material/fluidsystems/h2oairxylene.hh
View file @ 0ccde397
......@@ -348,7 +348,7 @@ public:
*/
Scalar muResult;
const Scalar mu[numComponents] = {
H2O::gasViscosity(fluidState.temperature(phaseIdx), H2O::vaporPressure(fluidState.temperature(phaseIdx))),
h2oGasViscosityInMixture(fluidState.temperature(phaseIdx),fluidState.pressure(phaseIdx)),
Air::gasViscosity(fluidState.temperature(phaseIdx), fluidState.pressure(phaseIdx)),
NAPL::gasViscosity(fluidState.temperature(phaseIdx), NAPL::vaporPressure(fluidState.temperature(phaseIdx)))
};
......
dumux/material/fluidsystems/h2oheavyoil.hh
View file @ 0ccde397
......@@ -337,7 +337,7 @@ public:
* -- compare e.g. with Promo Class p. 32/33
*/
const Scalar mu[numComponents] = {
H2O::gasViscosity(fluidState.temperature(phaseIdx), H2O::vaporPressure(fluidState.temperature(phaseIdx))),
h2oGasViscosityInMixture(fluidState.temperature(phaseIdx), fluidState.pressure(phaseIdx)),
HeavyOil::gasViscosity(fluidState.temperature(phaseIdx), HeavyOil::vaporPressure(fluidState.temperature(phaseIdx)))
};
......
dumux/material/fluidsystems/h2on2.hh
View file @ 0ccde397
......@@ -489,7 +489,7 @@ public:
// Wilke method (Reid et al.):
Scalar muResult = 0;
const Scalar mu[numComponents] = {
H2O::gasViscosity(T, H2O::vaporPressure(T)),
h2oGasViscosityInMixture(T, p),
N2::gasViscosity(T, p)
};
......
dumux/material/fluidsystems/h2on2o2.hh
View file @ 0ccde397
......@@ -563,7 +563,7 @@ public:
// Wilke method (Reid et al.):
Scalar muResult = 0;
const Scalar mu[numComponents] = {
H2O::gasViscosity(T, H2O::vaporPressure(T)),
h2oGasViscosityInMixture(T, p),
N2::gasViscosity(T, p),
O2::gasViscosity(T, p)
};
......
test/references/test_1pncminni_box-reference.vtu
View file @ 0ccde397
......@@ -7,10 +7,10 @@
200000 200000 200000 200000 200000 200000
</DataArray>
<DataArray type="Float32" Name="rho" NumberOfComponents="1" format="ascii">
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0.981785 0.981785 0.981785 0.981785 0.981785 0.981785
</DataArray>
<DataArray type="Float32" Name="mu" NumberOfComponents="1" format="ascii">
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</DataArray>
<DataArray type="Float32" Name="delp" NumberOfComponents="1" format="ascii">
100000 100000 100000 100000 100000 100000
......@@ -27,11 +27,11 @@
<DataArray type="Float32" Name="X^H2O_gas" NumberOfComponents="1" format="ascii">
0.357618 0.357618 0.357618 0.357618 0.357618 0.357618
</DataArray>
<DataArray type="Float32" Name="precipVolFrac_CaO" NumberOfComponents="1" format="ascii">
0.105174 0.105174 0.105174 0.105174 0.105174 0.105174
<DataArray type="Float32" Name="precipitateVolumeFraction^CaO" NumberOfComponents="1" format="ascii">
0.105328 0.105328 0.105328 0.105328 0.105328 0.105328
</DataArray>
<DataArray type="Float32" Name="precipVolFrac_CaOH2" NumberOfComponents="1" format="ascii">
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<DataArray type="Float32" Name="precipitateVolumeFraction^CaO2H2" NumberOfComponents="1" format="ascii">
0.0941565 0.0941565 0.0941565 0.0941565 0.0941565 0.0941565
</DataArray>
<DataArray type="Float32" Name="T" NumberOfComponents="1" format="ascii">
573.15 573.15 573.15 573.15 573.15 573.15
......@@ -40,10 +40,10 @@
8.53e-12 8.53e-12 8.53e-12 8.53e-12 8.53e-12 8.53e-12
</DataArray>
<DataArray type="Float32" Name="porosity" NumberOfComponents="1" format="ascii">
0.8 0.8 0.8 0.8 0.8 0.8
0.800516 0.800516 0.800516 0.800516 0.800516 0.800516
</DataArray>
<DataArray type="Float32" Name="reactionRate" NumberOfComponents="1" format="ascii">
7.84007 7.84007 7.84007 7.84007 7.84007 7.84007
7.8396 7.8396 7.8396 7.8396 7.8396 7.8396
</DataArray>
</PointData>
<CellData Scalars="process rank">
......
test/references/test_dec2p2c-reference.vtu
View file @ 0ccde397
This source diff could not be displayed because it is too large. You can view the blob instead.
test/references/test_md_boundary_darcy2p2c_stokes1p2c_horizontal_darcy-reference.vtu
View file @ 0ccde397
......@@ -4,18 +4,18 @@
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......@@ -24,22 +24,22 @@
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......@@ -60,18 +60,18 @@
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</DataArray>
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......@@ -88,16 +88,16 @@
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......@@ -128,31 +128,31 @@
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......
test/references/test_md_boundary_darcy2p2c_stokes1p2c_horizontal_stokes-reference.vtu
View file @ 0ccde397
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