Commit 6b6707de authored by Thomas Fetzer's avatar Thomas Fetzer Committed by Beatrix Becker
Browse files

[doc] Fix "coefficent" typo

parent 68658cfc
......@@ -50,7 +50,7 @@ public:
}
/*!
* \brief Binary diffusion coefficent \f$\mathrm{[m^2/s]}\f$ for air and mesitylene.
* \brief Binary diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for air and mesitylene.
* I used the method according to Wilke and Lee
* see W.J. Lyman, W.F. Reehl, D.H. Rosenblatt (1990) \cite lyman1990 <BR>
* \param temperature temperature in \f$\mathrm{[K]}\f$
......
......@@ -46,7 +46,7 @@ class Brine_Air {
public:
/*!
* \brief Binary diffusion coefficent \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$\mathrm{[K]}\f$
......@@ -67,7 +67,7 @@ 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 coefficent \f$\mathrm{[m^2/s]}\f$ for molecular nitrogen in liquid water.
* \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
......@@ -558,7 +558,7 @@ private:
}
/*!
* \brief The fugacity coefficent of Air for a Air-H2O mixture.
* \brief The fugacity coefficient of Air for a Air-H2O mixture.
*
* \param temperature the temperature [K]
* \param pg the gas phase pressure [Pa]
......
......@@ -541,7 +541,7 @@ private:
}
/*!
* \brief The fugacity coefficent of CO2 for a CO2-H2O mixture.
* \brief The fugacity coefficient of CO2 for a CO2-H2O mixture.
*
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pg the gas phase pressure \f$\mathrm{[Pa]}\f$
......
......@@ -31,7 +31,7 @@ namespace BinaryCoeff
{
/*!
* \ingroup Binarycoefficients
* \brief Estimate binary diffusion coefficents \f$\mathrm{[m^2/s]}\f$ in gases according to
* \brief Estimate binary diffusion coefficients \f$\mathrm{[m^2/s]}\f$ in gases according to
* the method by Fuller.
*
* \param M molar masses \f$\mathrm{[g/mol]}\f$
......@@ -39,7 +39,7 @@ namespace BinaryCoeff
* \param temperature The temperature \f$\mathrm{[K]}\f$
* \param pressure phase pressure \f$\mathrm{[Pa]}\f$
*
* This function estimates the diffusion coefficents in binary gases
* This function estimates the diffusion coefficients in binary gases
* using to the method proposed by Fuller. This method and is only
* valid at "low" pressures.
*
......
......@@ -39,7 +39,7 @@ class H2O_HeavyOil
{
public:
/*!
* \brief Henry coefficent \f$[N/m^2]\f$ for heavy oil in liquid water.
* \brief Henry coefficient \f$[N/m^2]\f$ for heavy oil in liquid water.
*
* See:
*
......@@ -55,7 +55,7 @@ public:
}
/*!
* \brief Henry coefficent \f$[N/m^2]\f$ for water in liquid heavy oil.
* \brief Henry coefficient \f$[N/m^2]\f$ for water in liquid heavy oil.
*
* See:
*
......@@ -70,7 +70,7 @@ public:
/*!
* \brief Binary diffusion coefficent [m^2/s] for molecular water and heavy oil.
* \brief Binary diffusion coefficient [m^2/s] for molecular water and heavy oil.
*
*/
template <class Scalar>
......@@ -80,7 +80,7 @@ public:
}
/*!
* \brief Diffusion coefficent [m^2/s] for tce in liquid water.
* \brief Diffusion coefficient [m^2/s] for tce in liquid water.
*
* \todo
*/
......
......@@ -39,7 +39,7 @@ class H2O_Mesitylene
{
public:
/*!
* \brief Henry coefficent \f$\mathrm{[Pa]}\f$ for mesitylene in liquid water.
* \brief Henry coefficient \f$\mathrm{[Pa]}\f$ for mesitylene in liquid water.
* \param temperature the temperature \f$\mathrm{[K]}\f$
* See:
*
......@@ -57,7 +57,7 @@ public:
}
/*!
* \brief Binary diffusion coefficent \f$\mathrm{[m^2/s]}\f$ for molecular water and mesitylene.
* \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$\mathrm{[Pa]}\f$
*
......@@ -107,7 +107,7 @@ public:
}
/*!
* \brief Diffusion coefficent \f$\mathrm{[m^2/s]}\f$ for mesitylene in liquid water.
* \brief Diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for mesitylene in liquid water.
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pressure the pressure \f$\mathrm{[Pa]}\f$
*
......
......@@ -43,7 +43,7 @@ class H2O_N2
{
public:
/*!
* \brief Henry coefficent \f$\mathrm{[Pa]}\f$ for molecular nitrogen in liquid water.
* \brief Henry coefficient \f$\mathrm{[Pa]}\f$ for molecular nitrogen in liquid water.
* \param temperature the temperature \f$\mathrm{[K]}\f$
*/
template <class Scalar>
......@@ -58,7 +58,7 @@ public:
}
/*!
* \brief Binary diffusion coefficent \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 nitrogen.
*
* 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 coefficent \f$\mathrm{[m^2/s]}\f$ for molecular nitrogen in liquid water.
* \brief Diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular nitrogen in liquid water.
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pressure the phase pressure \f$\mathrm{[Pa]}\f$
*
......
......@@ -43,7 +43,7 @@ class H2O_O2
{
public:
/*!
* \brief Henry coefficent \f$\mathrm{[Pa]}\f$ for molecular oxygen in liquid water.
* \brief Henry coefficient \f$\mathrm{[Pa]}\f$ for molecular oxygen in liquid water.
* \param temperature the temperature \f$\mathrm{[K]}\f$
*/
template <class Scalar>
......@@ -58,7 +58,7 @@ public:
}
/*!
* \brief Binary diffusion coefficent \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 nitrogen.
*
* 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 coefficent \f$\mathrm{[m^2/s]}\f$ for molecular nitrogen in liquid water.
* \brief Diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular nitrogen in liquid water.
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pressure the phase pressure \f$\mathrm{[Pa]}\f$
*
......
......@@ -39,7 +39,7 @@ class H2O_Xylene
{
public:
/*!
* \brief Henry coefficent \f$\mathrm{[Pa]}\f$ for xylene in liquid water.
* \brief Henry coefficient \f$\mathrm{[Pa]}\f$ for xylene in liquid water.
* \param temperature the temperature \f$\mathrm{[K]}\f$
*
* See:
......@@ -59,7 +59,7 @@ public:
}
/*!
* \brief Binary diffusion coefficent \f$\mathrm{[m^2/s]}\f$ for molecular water and xylene.
* \brief Binary diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular water and xylene.
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pressure the pressure \f$\mathrm{[Pa]}\f$
*
......@@ -107,7 +107,7 @@ public:
}
/*!
* \brief Diffusion coefficent \f$\mathrm{[m^2/s]}\f$ for xylene in liquid water.
* \brief Diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for xylene in liquid water.
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pressure the pressure \f$\mathrm{[Pa]}\f$
*
......
......@@ -43,7 +43,7 @@ class N2_O2
{
public:
/*!
* \brief Henry coefficent \f$\mathrm{[Pa]}\f$ for molecular oxygen in liquid nitrogen.
* \brief Henry coefficient \f$\mathrm{[Pa]}\f$ for molecular oxygen in liquid nitrogen.
* \param temperature the temperature \f$\mathrm{[K]}\f$
*/
template <class Scalar>
......@@ -53,7 +53,7 @@ public:
}
/*!
* \brief Binary diffusion coefficent \f$\mathrm{[m^2/s]}\f$ for molecular oxygen in liquid nitrogen.
* \brief Binary diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular oxygen in liquid nitrogen.
*
* Uses fullerMethod to determine the diffusion of water in nitrogen.
* \param temperature the temperature \f$\mathrm{[K]}\f$
......@@ -73,7 +73,7 @@ public:
}
/*!
* \brief Diffusion coefficent \f$\mathrm{[m^2/s]}\f$ for molecular oxygen in liquid nitrogen.
* \brief Diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular oxygen in liquid nitrogen.
* \param temperature the temperature \f$\mathrm{[K]}\f$
* \param pressure the phase pressure \f$\mathrm{[Pa]}\f$
*/
......
......@@ -133,12 +133,12 @@ public:
static const Scalar liquidEnthalpy(Scalar T,
Scalar p, Scalar salinity = constantSalinity)
{
/*Numerical coefficents from PALLISER*/
/*Numerical coefficients from PALLISER*/
static const Scalar f[] = {
2.63500E-1, 7.48368E-6, 1.44611E-6, -3.80860E-10
};
/*Numerical coefficents from MICHAELIDES for the enthalpy of brine*/
/*Numerical coefficients from MICHAELIDES for the enthalpy of brine*/
static const Scalar a[4][3] = {
{ +9633.6, -4080.0, +286.49 },
{ +166.58, +68.577, -4.6856 },
......
......@@ -466,7 +466,7 @@ public:
using Base::binaryDiffusionCoefficient;
/*!
* \brief Given the phase compositions, return the binary
* diffusion coefficent \f$\mathrm{[m^2/s]}\f$ of two components in a phase.
* diffusion coefficient \f$\mathrm{[m^2/s]}\f$ of two components in a phase.
* \param fluidState An arbitrary fluid state
* \param phaseIdx The index of the fluid phase to consider
* \param compIIdx Index of the component i
......
......@@ -353,7 +353,7 @@ public:
using Base::diffusionCoefficient;
/*!
* \brief Given all mole fractions, return the diffusion
* coefficent in \f$\mathrm{[m^2/s]}\f$ of a component in a phase.
* coefficient in \f$\mathrm{[m^2/s]}\f$ of a component in a phase.
* \param fluidState The fluid state
* \param phaseIdx The index of the phase
* \param compIdx The index of the component
......
......@@ -352,7 +352,7 @@ public:
using Base::diffusionCoefficient;
/*!
* \brief Given all mole fractions, return the diffusion
* coefficent \f$\mathrm{[m^2/s]}\f$ of a component in a phase.
* coefficient \f$\mathrm{[m^2/s]}\f$ of a component in a phase.
* \param fluidState The fluid state
* \param phaseIdx The index of the phase to consider
* \param compIdx The index of the component to consider
......
......@@ -133,7 +133,7 @@ public:
*/
static bool isIdealMixture(int phaseIdx)
{
// always use the reference oil for the fugacity coefficents,
// always use the reference oil for the fugacity coefficients,
// so they cannot be dependent on composition and they the
// phases thus always an ideal mixture
return phaseIdx == wPhaseIdx;
......
......@@ -146,7 +146,7 @@ public:
int compIIdx = phaseIdx;
for (unsigned int compJIdx = 0; compJIdx < numComponents; ++compJIdx)
{
// binary diffusion coefficents
// binary diffusion coefficients
if(compIIdx!= compJIdx)
{
setDiffusionCoefficient_(phaseIdx, compJIdx,
......
......@@ -215,7 +215,7 @@ private:
for (int phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx)
{
// make sure to calculate only diffusion coefficents
// make sure to calculate only diffusion coefficients
// for phases which exist in both finite volumes
/* \todo take care: This should be discussed once again
* as long as a meaningful value can be found for the required mole fraction
......
......@@ -678,7 +678,7 @@ public:
* for the porous media happens at another place!
*/
// diffusivity coefficents
// diffusivity coefficients
diffusionCoefficient_[gPhaseIdx] = FluidSystem::diffusionCoefficient(fluidState_, gPhaseIdx);
diffusionCoefficient_[wPhaseIdx] = FluidSystem::diffusionCoefficient(fluidState_, wPhaseIdx);
......
......@@ -312,7 +312,7 @@ public:
ParentType::relativePermeability_[phaseIdx] = kr;
Valgrind::CheckDefined(ParentType::relativePermeability_[phaseIdx]);
// binary diffusion coefficents
// binary diffusion coefficients
ParentType::diffCoeff_[phaseIdx] =
FluidSystem::binaryDiffusionCoefficient(ParentType::fluidState_,
paramCache,
......
......@@ -127,7 +127,7 @@ public:
// point in the porous medium
for (int phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx)
{
// make sure to only calculate diffusion coefficents
// make sure to only calculate diffusion coefficients
// for phases which exist in both finite volumes
if (elemVolVars[i].saturation(phaseIdx) <= 1e-4 ||
elemVolVars[j].saturation(phaseIdx) <= 1e-4)
......
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