Commit 4b29de73 authored by Simon Scholz's avatar Simon Scholz
Browse files

Merge branch 'fix/doxy-material' into 'next'

Fix/doxy material

See merge request !701
parents bc592548 d9a59563
......@@ -7,6 +7,8 @@ brine_air.hh
brine_co2.hh
fullermethod.hh
h2o_air.hh
h2o_constant.hh
h2o_heavyoil.hh
h2o_mesitylene.hh
h2o_n2.hh
h2o_o2.hh
......
......@@ -18,7 +18,7 @@
*****************************************************************************/
/*!
* \file
*
* \ingroup Binarycoefficients
* \brief Binary coefficients for air and mesitylene.
*/
#ifndef DUMUX_BINARY_COEFF_AIR_MESITYLENE_HH
......@@ -33,15 +33,15 @@ namespace BinaryCoeff
{
/*!
* \ingroup Binarycoefficients
* \brief Binary coefficients for water and mesitylene.
* \param temperature temperature in \f$\mathrm{[K]}\f$
*
*/
class Air_Mesitylene
{
public:
/*!
*
* \brief Henry coefficient \f$\mathrm{[Pa]}\f$ for mesitylene in air.
* \param temperature the temperature \f$\mathrm{[K]}\f$
*/
template <class Scalar>
static Scalar henry(Scalar temperature)
......
......@@ -18,7 +18,7 @@
*****************************************************************************/
/*!
* \file
*
* \ingroup Binarycoefficients
* \brief Binary coefficients for air and xylene.
*/
#ifndef DUMUX_BINARY_COEFF_AIR_XYLENE_HH
......@@ -33,15 +33,15 @@ namespace BinaryCoeff
{
/*!
* \brief Binary coefficients for water and xylene.
* \param temperature temperature in \f$\mathrm{[K]}\f$
*
* \ingroup Binarycoefficients
* \brief Binary coefficients for air and xylene.
*/
class Air_Xylene
{
public:
/*!
*
* \brief Henry coefficient \f$\mathrm{[Pa]}\f$ for mesitylene in air.
* \param temperature the temperature \f$\mathrm{[K]}\f$
*/
template <class Scalar>
static Scalar henry(Scalar temperature)
......
......@@ -18,9 +18,8 @@
*****************************************************************************/
/*!
* \file
*
* \ingroup Binarycoefficients
* \brief Binary coefficients for Air and brine.
* \brief Binary coefficients for Brine and Air.
*/
#ifndef DUMUX_BINARY_COEFF_BRINE_Air_HH
#define DUMUX_BINARY_COEFF_BRINE_Air_HH
......@@ -33,7 +32,8 @@
namespace Dumux {
namespace BinaryCoeff {
/*!
* \brief Binary coefficients for brine and Air.
* \ingroup Binarycoefficients
* \brief Binary coefficients for Brine and Air.
*/
template<class Scalar, class Air, bool verbose = true>
class Brine_Air {
......@@ -41,12 +41,12 @@ class Brine_Air {
// using Air = Dumux::Air<Scalar>;
using Brine = Dumux::Brine<Scalar,H2O>;
using IdealGas = Dumux::IdealGas<Scalar>;
static const int lPhaseIdx = 0; // index of the liquid phase
static const int gPhaseIdx = 1; // index of the gas phase
static const int wPhaseIdx = 0; // index of the liquid phase
static const int nPhaseIdx = 1; // index of the gas phase
public:
/*!
* \brief Binary diffusion coefficient \f$\mathrm{[m^2/s]}\f$ of water in the Air phase.
* \brief Binary diffusion coefficient \f$\mathrm{[m^2/s]}\f$ of water in the Air phase.
*
* According to B. Xu et al. (2003) \cite xu2003 <BR>
* \param temperature the temperature \f$\mathrm{[K]}\f$
......@@ -65,24 +65,24 @@ public:
;
/*!
* Lacking better data on water-air diffusion in liquids, we use at the
* moment the diffusion coefficient of the air's main component nitrogen!!
* \brief Diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular nitrogen in liquid water.
*
* The empirical equations for estimating the diffusion coefficient in
* infinite solution which are presented in Reid, 1987 all show a
* linear dependency on temperature. We thus simply scale the
* experimentally obtained diffusion coefficient of Ferrell and
* Himmelblau by the temperature.
* \param temperature The temperature \f$\mathrm{[K]}\f$
* \param pressure The pressure \f$\mathrm{[Pa]}\f$
*
* See:
*
* R. Reid et al. (1987, pp. 599) \cite reid1987 <BR>
*
* R. Ferrell, D. Himmelblau (1967, pp. 111-115) \cite ferrell1967
*/
* Lacking better data on water-air diffusion in liquids, we use at the
* moment the diffusion coefficient of the air's main component nitrogen!!
* \brief Diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular nitrogen in liquid water.
*
* The empirical equations for estimating the diffusion coefficient in
* infinite solution which are presented in Reid, 1987 all show a
* linear dependency on temperature. We thus simply scale the
* experimentally obtained diffusion coefficient of Ferrell and
* Himmelblau by the temperature.
* \param temperature The temperature \f$\mathrm{[K]}\f$
* \param pressure The pressure \f$\mathrm{[Pa]}\f$
*
* See:
*
* R. Reid et al. (1987, pp. 599) \cite reid1987 <BR>
*
* R. Ferrell, D. Himmelblau (1967, pp. 111-115) \cite ferrell1967
*/
static Scalar liquidDiffCoeff(Scalar temperature, Scalar pressure) {
//Diffusion coefficient of Air in the H2O phase
const Scalar Texp = 273.15 + 25; // [K]
......@@ -94,7 +94,7 @@ public:
* \brief Returns the _mol_ (!) fraction of Air in the liquid
* phase and the mol_ (!) fraction of H2O in the gas phase
* for a given temperature, pressure, Air density and brine
* XlNaCl.
* XwNaCl.
*
* Implemented according to Spycher and Pruess (2005) \cite spycher2005 <BR>
* applying the activity coefficient expression of Duan and Sun (2003) \cite duan2003 <BR>
......@@ -102,52 +102,52 @@ public:
*
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pg the gas phase pressure \f$\mathrm{[Pa]}\f$
* \param XlNaCl the XlNaCl \f$\mathrm{[kg NaCl / kg solution]}\f$
* \param XwNaCl the XwNaCl \f$\mathrm{[kg NaCl / kg solution]}\f$
* \param knownPhaseIdx indicates which phases are present
* \param xlAir mole fraction of Air in brine \f$\mathrm{[mol/mol]}\f$
* \param ygH2O mole fraction of water in the gas phase \f$\mathrm{[mol/mol]}\f$
* \param xlNaCl the xlNaCl
* \param xwAir mole fraction of Air in brine \f$\mathrm{[mol/mol]}\f$
* \param xnH2O mole fraction of water in the gas phase \f$\mathrm{[mol/mol]}\f$
* \param xwNaCl the xwNaCl
*/
static void calculateMoleFractions(const Scalar temperature,
const Scalar pg,
const Scalar XlNaCl,
const Scalar XwNaCl,
const int knownPhaseIdx,
Scalar &xlAir,
Scalar &ygH2O,
Scalar &xlNaCl) {
Scalar &xwAir,
Scalar &xnH2O,
Scalar &xwNaCl) {
DUNE_THROW(Dune::InvalidStateException, "Function: " << "calculateMoleFractions" << " is invalid.");
// Scalar A = computeA_(temperature, pg);
//
// /* XlNaCl: conversion from mass fraction to mol fraction */
// xlNaCl = massTomoleFrac_(XlNaCl);
// /* XwNaCl: conversion from mass fraction to mol fraction */
// xwNaCl = massTomoleFrac_(XwNaCl);
//
// // if both phases are present the mole fractions in each phase can be calculate
// // with the mutual solubility function
// if (knownPhaseIdx < 0) {
// Scalar molalityNaCl = molFracToMolality_(xlNaCl); // molality of NaCl //CHANGED
// Scalar molalityNaCl = molFracToMolality_(xwNaCl); // molality of NaCl //CHANGED
// Scalar m0_Air = molalityAirinPureWater_(temperature, pg); // molality of Air in pure water
// Scalar gammaStar = activityCoefficient_(temperature, pg, molalityNaCl);// activity coefficient of Air in brine
// Scalar m_Air = m0_Air / gammaStar; // molality of Air in brine
// xlAir = m_Air / (molalityNaCl + 55.508 + m_Air); // mole fraction of Air in brine
// ygH2O = A * (1 - xlAir - xlNaCl); // mole fraction of water in the gas phase
// xwAir = m_Air / (molalityNaCl + 55.508 + m_Air); // mole fraction of Air in brine
// xnH2O = A * (1 - xwAir - xwNaCl); // mole fraction of water in the gas phase
// }
//
// // if only liquid phase is present the mole fraction of Air in brine is given and
// // and the virtual equilibrium mole fraction of water in the non-existing gas phase can be estimated
// // with the mutual solubility function
// if (knownPhaseIdx == lPhaseIdx) {
//// ygH2O = A * (1 - xlAir - xlNaCl);
// DUNE_THROW(Dune::InvalidStateException, "phase index: " << "lPhaseIdx" << " is invalid.");
// if (knownPhaseIdx == wPhaseIdx) {
//// xnH2O = A * (1 - xwAir - xwNaCl);
// DUNE_THROW(Dune::InvalidStateException, "phase index: " << "wPhaseIdx" << " is invalid.");
//
// }
//
// // if only gas phase is present the mole fraction of water in the gas phase is given and
// // and the virtual equilibrium mole fraction of Air in the non-existing liquid phase can be estimated
// // with the mutual solubility function
// if (knownPhaseIdx == gPhaseIdx) {
// if (knownPhaseIdx == nPhaseIdx) {
// //y_H2o = fluidstate.
//// xlAir = 1 - xlNaCl - ygH2O / A;
// DUNE_THROW(Dune::InvalidStateException, "phase index: " << "gPhaseIdx" << " is invalid.");
//// xwAir = 1 - xwNaCl - xnH2O / A;
// DUNE_THROW(Dune::InvalidStateException, "phase index: " << "nPhaseIdx" << " is invalid.");
// }
}
......@@ -212,12 +212,12 @@ public:
/*!
* \brief Returns the molality of NaCl \f$\mathrm{(mol NaCl / kg water)}\f$ for a given mole fraction \f$\mathrm{(mol NaCl / mol solution)}\f$
*
* \param XlNaCl mole fraction of NaCL in brine \f$\mathrm{[mol/mol]}\f$
* \param XwNaCl mole fraction of NaCL in brine \f$\mathrm{[mol/mol]}\f$
*/
static Scalar molalityNaCl(Scalar XlNaCl) {
static Scalar molalityNaCl(Scalar XwNaCl) {
// conversion from mol fraction to molality
const Scalar mol_NaCl = XlNaCl / 58.4428e-3;
const Scalar mol_NaCl = XwNaCl / 58.4428e-3;
return mol_NaCl;
}
......@@ -226,19 +226,19 @@ private:
/*!
* \brief Returns the molality of NaCl \f$\mathrm{(mol NaCl / kg water)}\f$ for a given mole fraction
*
* \param XlNaCl the XlNaCl \f$\mathrm{[kg NaCl / kg solution]}\f$
* \param XwNaCl the XwNaCl \f$\mathrm{[kg NaCl / kg solution]}\f$
*/
static Scalar massTomoleFrac_(Scalar XlNaCl) {
static Scalar massTomoleFrac_(Scalar XwNaCl) {
DUNE_THROW(Dune::InvalidStateException, "Function: " << "massTomoleFrac_" << " is invalid.");
// const Scalar Mw = H2O::molarMass(); /* molecular weight of water [kg/mol] */
// const Scalar Ms = 58.8e-3; /* molecular weight of NaCl [kg/mol] */
//
// const Scalar X_NaCl = XlNaCl;
// /* XlNaCl: conversion from mass fraction to mol fraction */
// const Scalar xlNaCl = -Mw * X_NaCl / ((Ms - Mw) * X_NaCl - Ms);
// return xlNaCl;
// const Scalar X_NaCl = XwNaCl;
// /* XwNaCl: conversion from mass fraction to mol fraction */
// const Scalar xwNaCl = -Mw * X_NaCl / ((Ms - Mw) * X_NaCl - Ms);
// return xwNaCl;
}
/*!
......@@ -431,12 +431,12 @@ public:
const Scalar Mw = H2O::molarMass(); /* molecular weight of water [kg/mol] */
const Scalar Ms = 58.8e-3; /* molecular weight of NaCl [kg/mol] */
const Scalar X_NaCl = Brine::XlNaCl;
/* XlNaCl: conversion from mass fraction to mole fraction */
const Scalar xlNaCl = -Mw * X_NaCl / ((Ms - Mw) * X_NaCl - Ms);
const Scalar X_NaCl = Brine::XwNaCl;
/* XwNaCl: conversion from mass fraction to mole fraction */
const Scalar xwNaCl = -Mw * X_NaCl / ((Ms - Mw) * X_NaCl - Ms);
// XlNaCl: conversion from mole fraction to molality
const Scalar mol_NaCl = -55.56 * xlNaCl / (xlNaCl - 1);
// XwNaCl: conversion from mole fraction to molality
const Scalar mol_NaCl = -55.56 * xwNaCl / (xwNaCl - 1);
const Scalar A = computeA_(temperature, pg); /* mu_{Air}^{l(0)}/RT */
const Scalar B = computeB_(temperature, pg); /* lambda_{Air-Na+} */
......@@ -459,10 +459,10 @@ public:
private:
/*!
* \brief computation of mu_{Air}^{l(0)}/RT
* \param T the temperature [K]
* \param pg the gas phase pressure [Pa]
*/
* \brief computation of mu_{Air}^{l(0)}/RT
* \param T the temperature [K]
* \param pg the gas phase pressure [Pa]
*/
static Scalar computeA_(Scalar T, Scalar pg)
{
static const Scalar c[10] = {
......@@ -564,7 +564,6 @@ private:
* \param pg the gas phase pressure [Pa]
* \param rhoAir the density of Air for the critical volume [kg/m^3]
*/
static Scalar fugacityCoeffAir_(Scalar temperature,
Scalar pg,
Scalar rhoAir)
......
......@@ -18,7 +18,6 @@
*****************************************************************************/
/*!
* \file
*
* \ingroup Binarycoefficients
* \brief Binary coefficients for CO2 and brine.
*/
......@@ -33,6 +32,7 @@
namespace Dumux {
namespace BinaryCoeff {
/*!
* \ingroup Binarycoefficients
* \brief Binary coefficients for brine and CO2.
*/
template<class Scalar, class CO2Tables, bool verbose = true>
......@@ -92,7 +92,6 @@ public:
* \param xlCO2 mole fraction of CO2 in brine \f$\mathrm{[mol/mol]}\f$
* \param ygH2O mole fraction of water in the gas phase \f$\mathrm{[mol/mol]}\f$
*/
static void calculateMoleFractions(const Scalar temperature,
const Scalar pg,
const Scalar salinity,
......@@ -442,10 +441,10 @@ public:
private:
/*!
* \brief computation of \f$\mathrm{[mu_{CO2}^{l(0)}/RT]}\f$
* \brief computation of \f$\mathrm{[mu_{CO2}^{l(0)}/RT]}\f$
* \param T the temperature \f$\mathrm{[K]}\f$
* \param pg the gas phase pressure \f$\mathrm{[Pa]}\f$
*/
*/
static Scalar computeA_(Scalar T, Scalar pg)
{
static const Scalar c[10] = {
......@@ -504,6 +503,7 @@ private:
c9*pg_bar/(630.0-T) +
c11*T*log(pg_bar);
}
/*!
* \brief computation of C
*
......@@ -525,6 +525,7 @@ private:
c8*pg_bar/T +
c9*pg_bar/(630.0-T);
}
/*!
* \brief computation of partial pressure CO2
*
......@@ -547,7 +548,6 @@ private:
* \param pg the gas phase pressure \f$\mathrm{[Pa]}\f$
* \param rhoCO2 the density of CO2 for the critical volume \f$\mathrm{[kg/m^3]}\f$
*/
static Scalar fugacityCoeffCO2_(Scalar temperature,
Scalar pg,
Scalar rhoCO2)
......
......@@ -18,7 +18,9 @@
*****************************************************************************/
/*!
* \file
* \ingroup Binarycoefficients
* \brief Various relations for molecular diffusion coefficients.
* \copydetails fullerMethod
*/
#ifndef DUMUX_FULLERMETHOD_HH
#define DUMUX_FULLERMETHOD_HH
......@@ -30,7 +32,6 @@ namespace Dumux
namespace BinaryCoeff
{
/*!
* \ingroup Binarycoefficients
* \brief Estimate binary diffusion coefficients \f$\mathrm{[m^2/s]}\f$ in gases according to
* the method by Fuller.
*
......
......@@ -18,8 +18,8 @@
*****************************************************************************/
/*!
* \file
*
* \brief Binary coefficients for water and nitrogen.
* \ingroup Binarycoefficients
* \brief Binary coefficients for water and air.
*/
#ifndef DUMUX_BINARY_COEFF_H2O_AIR_HH
#define DUMUX_BINARY_COEFF_H2O_AIR_HH
......@@ -34,7 +34,7 @@ namespace BinaryCoeff
/*!
* \ingroup Binarycoefficients
* \brief Binary coefficients for water and nitrogen.
* \brief Binary coefficients for water and air.
*/
class H2O_Air
{
......
......@@ -18,7 +18,7 @@
*****************************************************************************/
/*!
* \file
*
* \ingroup Binarycoefficients
* \brief Binary coefficients for water and a "constant" component.
*/
#ifndef DUMUX_BINARY_COEFF_H2O_CONSTANT_HH
......@@ -37,6 +37,7 @@ namespace BinaryCoeff
{
/*!
* \ingroup Binarycoefficients
* \brief Binary coefficients for water and another component.
* \todo All other binary coefficient could be generalized like this
*/
......@@ -58,12 +59,10 @@ class H2O_Component<Scalar, Components::Constant<id, Scalar>>
{
public:
/*!
* \brief Henry coefficent \f$N/m^2\f$ for heavy oil in liquid water.
*
* See:
* \brief Henry coefficent \f$N/m^2\f$ for the constant component in liquid water.
*
* \param temperature the temperature \f$\mathrm{[K]}\f$
*/
static Scalar henryCompInWater(Scalar temperature)
{
static const Scalar h = getParamFromGroup<Scalar>(std::to_string(id), "Component.HenryComponentInWater", 1.0);
......@@ -71,12 +70,10 @@ public:
}
/*!
* \brief Henry coefficent \f$N/m^2\f$ for water in liquid heavy oil.
*
* See:
* \brief Henry coefficent \f$N/m^2\f$ for water in the constant component.
*
* \param temperature the temperature \f$\mathrm{[K]}\f$
*/
static Scalar henryWaterInComp(Scalar temperature)
{
static const Scalar h = getParamFromGroup<Scalar>(std::to_string(id), "Component.HenryWaterInComponent", 1.0);
......@@ -85,8 +82,9 @@ public:
/*!
* \brief Binary diffusion coefficent \f$m^2/s\f$ for molecular water and heavy oil.
*
* \brief Binary diffusion coefficent \f$m^2/s\f$ for molecular water and the constant component.
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pressure the phase pressure \f$\mathrm{[Pa]}\f$
*/
static Scalar gasDiffCoeff(Scalar temperature, Scalar pressure)
{
......@@ -95,9 +93,9 @@ public:
}
/*!
* \brief Diffusion coefficent \f$m^2/s\f$ for tce in liquid water.
*
* \todo
* \brief Diffusion coefficent \f$m^2/s\f$ for the constant component in liquid water.
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pressure the phase pressure \f$\mathrm{[Pa]}\f$
*/
static Scalar liquidDiffCoeff(Scalar temperature, Scalar pressure)
{
......
......@@ -18,8 +18,8 @@
*****************************************************************************/
/*!
* \file
*
* \brief Binary coefficients for water and tce.
* \ingroup Binarycoefficients
* \brief Binary coefficients for water and heavy oil.
*/
#ifndef DUMUX_BINARY_COEFF_H2O_HEAVYOIL_HH
#define DUMUX_BINARY_COEFF_H2O_HEAVYOIL_HH
......@@ -33,6 +33,7 @@ namespace BinaryCoeff
{
/*!
* \ingroup Binarycoefficients
* \brief Binary coefficients for water and heavy oil as in SAGD processes
*/
class H2O_HeavyOil
......@@ -40,11 +41,8 @@ class H2O_HeavyOil
public:
/*!
* \brief Henry coefficient \f$[N/m^2]\f$ for heavy oil in liquid water.
*
* See:
*
* \param temperature the temperature \f$\mathrm{[K]}\f$
*/
template <class Scalar>
static Scalar henryOilInWater(Scalar temperature)
{
......@@ -56,11 +54,8 @@ public:
/*!
* \brief Henry coefficient \f$[N/m^2]\f$ for water in liquid heavy oil.
*
* See:
*
* \param temperature the temperature \f$\mathrm{[K]}\f$
*/
template <class Scalar>
static Scalar henryWaterInOil(Scalar temperature)
{
......@@ -71,7 +66,8 @@ public:
/*!
* \brief Binary diffusion coefficient [m^2/s] for molecular water and heavy oil.
*
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pressure the phase pressure \f$\mathrm{[Pa]}\f$
*/
template <class Scalar>
static Scalar gasDiffCoeff(Scalar temperature, Scalar pressure)
......@@ -80,9 +76,9 @@ public:
}
/*!
* \brief Diffusion coefficient [m^2/s] for tce in liquid water.
*
* \todo
* \brief Diffusion coefficient [m^2/s] for heavy oil in liquid water.
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pressure the phase pressure \f$\mathrm{[Pa]}\f$
*/
template <class Scalar>
static Scalar liquidDiffCoeff(Scalar temperature, Scalar pressure)
......
......@@ -18,7 +18,7 @@
*****************************************************************************/
/*!
* \file
*
* \ingroup Binarycoefficients
* \brief Binary coefficients for water and mesitylene.
*/
#ifndef DUMUX_BINARY_COEFF_H2O_MESITYLENE_HH
......@@ -33,6 +33,7 @@ namespace BinaryCoeff
{
/*!
* \ingroup Binarycoefficients
* \brief Binary coefficients for water and mesitylene.
*/
class H2O_Mesitylene
......@@ -42,8 +43,7 @@ public:
* \brief Henry coefficient \f$\mathrm{[Pa]}\f$ for mesitylene in liquid water.
* \param temperature the temperature \f$\mathrm{[K]}\f$
* See:
*
* R. Sander (1999) \cite sander1999
* R. Sander (1999) \cite sander1999
*/
template <class Scalar>
static Scalar henry(Scalar temperature)
......@@ -60,7 +60,6 @@ public:
* \brief Binary diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular water and mesitylene.
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pressure the pressure \f$\mathrm{[Pa]}\f$
*
*/
template <class Scalar>
static Scalar gasDiffCoeff(Scalar temperature, Scalar pressure)
......
......@@ -18,7 +18,7 @@
*****************************************************************************/
/*!
* \file
*
* \ingroup Binarycoefficients
* \brief Binary coefficients for water and nitrogen.
*/
#ifndef DUMUX_BINARY_COEFF_H2O_N2_HH
......
......@@ -18,7 +18,7 @@
*****************************************************************************/
/*!
* \file
*
* \ingroup Binarycoefficients
* \brief Binary coefficients for water and oxygen.
*/
#ifndef DUMUX_BINARY_COEFF_H2O_O2_HH
......@@ -58,7 +58,7 @@ public:
}
/*!
* \brief Binary diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular water and nitrogen.
* \brief Binary diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular water and oxygen.
*
* Uses fullerMethod to determine the diffusion of water in nitrogen.
* \param temperature the temperature \f$\mathrm{[K]}\f$
......@@ -79,7 +79,7 @@ public:
}
/*!
* \brief Diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular nitrogen in liquid water.
* \brief Diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular oxygen in liquid water.
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pressure the phase pressure \f$\mathrm{[Pa]}\f$
*
......
......@@ -18,7 +18,7 @@
*****************************************************************************/
/*!
* \file
*
* \ingroup Binarycoefficients
* \brief Binary coefficients for water and xylene.
*/
#ifndef DUMUX_BINARY_COEFF_H2O_XYLENE_HH
......@@ -33,6 +33,7 @@ namespace BinaryCoeff
{