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10 commits

Author SHA1 Message Date
Yeongdo Park
01b0b1396b Update .gitlab-ci.yml 2018-10-31 15:46:39 +00:00
Yeongdo Park
9f1a9c60d1 Update .gitlab-ci.yml 2018-10-31 14:27:04 +00:00
Yeongdo Park
75c8f48c51 update CI Lint for new GitLab Runner 2018-10-25 07:31:35 -04:00
ignis
b5bebc52ec New methods for all species Cp and Cv 2018-07-10 15:24:03 +09:00
ignis
6b3e8c972b Qc and Qc2 field calculation dimension correctly set 2018-07-10 14:59:50 +09:00
ignis
8670f39b9f specie and specieMixtures feature for electrical property calculation 2018-04-25 14:56:01 +09:00
ignis
c06d324891 mixture got specific charge field calculation 2018-04-19 13:39:45 +09:00
ignis
3efddbac8a new attr nCharges_ and related methods of specie and chemkinReader mod for cation name 2018-04-18 11:09:25 +09:00
Yeongdo Park
ad1db37d45 Merge branch 'EvaporationModels' into 'trunk'
added convection-diffusion-controlled liquid evaporation model

See merge request combustion-postech/OpenFOAM-4.x!10
2018-01-20 21:42:17 +00:00
Dohyun Kim
408cd2c2d3 Evaporation models 2018-01-20 21:40:15 +00:00
23 changed files with 875 additions and 28 deletions

View file

@ -1,9 +1,23 @@
before_script:
- "[[ -d ../ThirdParty-4.x ]] || git clone https://github.com/OpenFOAM/ThirdParty-4.x.git ../ThirdParty-4.x"
- source etc/bashrc
- rm -rf platforms
- wclean all
allmake:
image: park0d/of4builder
tags:
- openfoam4
before_script:
- "[[ -d ../ThirdParty-4.x ]] || git clone https://github.com/OpenFOAM/ThirdParty-4.x.git ../ThirdParty-4.x"
- source etc/bashrc
- rm -rf platforms
- wclean all
script:
- ./Allwmake -j
artifacts:
paths:
- ./
cantera:
image: park0d/of4builder
tags:
- openfoam4
script:
- whereis libcantera

View file

@ -96,7 +96,8 @@ void Foam::ReactingParcel<ParcelType>::calcPhaseChange
pc_,
this->Tc_,
X,
dMassPC
dMassPC,
this->rhoc_
);
// Limit phase change mass by availability of each specie

View file

@ -30,6 +30,7 @@ License
#include "NoPhaseChange.H"
#include "LiquidEvaporation.H"
#include "LiquidEvaporationConvDiff.H"
#include "LiquidEvaporationBoil.H"
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
@ -39,6 +40,7 @@ License
makePhaseChangeModel(CloudType); \
makePhaseChangeModelType(NoPhaseChange, CloudType); \
makePhaseChangeModelType(LiquidEvaporation, CloudType); \
makePhaseChangeModelType(LiquidEvaporationConvDiff, CloudType); \
makePhaseChangeModelType(LiquidEvaporationBoil, CloudType);

View file

@ -142,7 +142,8 @@ void Foam::LiquidEvaporation<CloudType>::calculate
const scalar pc,
const scalar Tc,
const scalarField& X,
scalarField& dMassPC
scalarField& dMassPC,
const scalar rhoc
) const
{
// immediately evaporate mass that has reached critical condition
@ -196,8 +197,8 @@ void Foam::LiquidEvaporation<CloudType>::calculate
// vapour concentration at surface [kmol/m3] at film temperature
const scalar Cs = pSat/(RR*Ts);
// vapour concentration in bulk gas [kmol/m3] at film temperature
const scalar Cinf = Xc[gid]*pc/(RR*Ts);
// vapour concentration in bulk gas [kmol/m3] at bulk gas temperature
const scalar Cinf = Xc[gid]*pc/(RR*Tc);
// molar flux of vapour [kmol/m2/s]
const scalar Ni = max(kc*(Cs - Cinf), 0.0);

View file

@ -119,7 +119,8 @@ public:
const scalar pc,
const scalar Tc,
const scalarField& X,
scalarField& dMassPC
scalarField& dMassPC,
const scalar rhoc
) const;
//- Return the enthalpy per unit mass

View file

@ -142,7 +142,8 @@ void Foam::LiquidEvaporationBoil<CloudType>::calculate
const scalar pc,
const scalar Tc,
const scalarField& X,
scalarField& dMassPC
scalarField& dMassPC,
const scalar rhoc
) const
{
// immediately evaporate mass that has reached critical condition

View file

@ -129,7 +129,8 @@ public:
const scalar pc,
const scalar Tc,
const scalarField& X,
scalarField& dMassPC
scalarField& dMassPC,
const scalar rhoc
) const;
//- Return the enthalpy per unit mass

View file

@ -0,0 +1,287 @@
/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | Copyright (C) 2011-2016 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
This file is part of OpenFOAM.
OpenFOAM is free software: you can redistribute it and/or modify it
under the terms of the GNU General Public License as published by
the Free Software Foundation, either version 3 of the License, or
(at your option) any later version.
OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License
for more details.
You should have received a copy of the GNU General Public License
along with OpenFOAM. If not, see <http://www.gnu.org/licenses/>.
\*---------------------------------------------------------------------------*/
#include "LiquidEvaporationConvDiff.H"
#include "specie.H"
#include "mathematicalConstants.H"
using namespace Foam::constant::mathematical;
// * * * * * * * * * * * * * Private Member Functions * * * * * * * * * * * //
template<class CloudType>
Foam::tmp<Foam::scalarField> Foam::LiquidEvaporationConvDiff<CloudType>::calcXc
(
const label celli
) const
{
scalarField Xc(this->owner().thermo().carrier().Y().size());
forAll(Xc, i)
{
Xc[i] =
this->owner().thermo().carrier().Y()[i][celli]
/this->owner().thermo().carrier().W(i);
}
return Xc/sum(Xc);
}
template<class CloudType>
Foam::scalar Foam::LiquidEvaporationConvDiff<CloudType>::Sh
(
const scalar Re,
const scalar Sc
) const
{
return 2.0 + 0.6*Foam::sqrt(Re)*cbrt(Sc);
}
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
template<class CloudType>
Foam::LiquidEvaporationConvDiff<CloudType>::LiquidEvaporationConvDiff
(
const dictionary& dict,
CloudType& owner
)
:
PhaseChangeModel<CloudType>(dict, owner, typeName),
liquids_(owner.thermo().liquids()),
activeLiquids_(this->coeffDict().lookup("activeLiquids")),
liqToCarrierMap_(activeLiquids_.size(), -1),
liqToLiqMap_(activeLiquids_.size(), -1)
{
if (activeLiquids_.size() == 0)
{
WarningInFunction
<< "Evaporation model selected, but no active liquids defined"
<< nl << endl;
}
else
{
Info<< "Participating liquid species:" << endl;
// Determine mapping between liquid and carrier phase species
forAll(activeLiquids_, i)
{
Info<< " " << activeLiquids_[i] << endl;
liqToCarrierMap_[i] =
owner.composition().carrierId(activeLiquids_[i]);
}
// Determine mapping between model active liquids and global liquids
const label idLiquid = owner.composition().idLiquid();
forAll(activeLiquids_, i)
{
liqToLiqMap_[i] =
owner.composition().localId(idLiquid, activeLiquids_[i]);
}
}
}
template<class CloudType>
Foam::LiquidEvaporationConvDiff<CloudType>::LiquidEvaporationConvDiff
(
const LiquidEvaporationConvDiff<CloudType>& pcm
)
:
PhaseChangeModel<CloudType>(pcm),
liquids_(pcm.owner().thermo().liquids()),
activeLiquids_(pcm.activeLiquids_),
liqToCarrierMap_(pcm.liqToCarrierMap_),
liqToLiqMap_(pcm.liqToLiqMap_)
{}
// * * * * * * * * * * * * * * * * Destructor * * * * * * * * * * * * * * * //
template<class CloudType>
Foam::LiquidEvaporationConvDiff<CloudType>::~LiquidEvaporationConvDiff()
{}
// * * * * * * * * * * * * * * * Member Functions * * * * * * * * * * * * * //
template<class CloudType>
void Foam::LiquidEvaporationConvDiff<CloudType>::calculate
(
const scalar dt,
const label celli,
const scalar Re,
const scalar Pr,
const scalar d,
const scalar nu,
const scalar T,
const scalar Ts,
const scalar pc,
const scalar Tc,
const scalarField& X,
scalarField& dMassPC,
const scalar rhoc //POSECH
) const
{
// immediately evaporate mass that has reached critical condition
if ((liquids_.Tc(X) - T) < SMALL)
{
if (debug)
{
WarningInFunction
<< "Parcel reached critical conditions: "
<< "evaporating all avaliable mass" << endl;
}
forAll(activeLiquids_, i)
{
const label lid = liqToLiqMap_[i];
dMassPC[lid] = GREAT;
}
return;
}
// construct carrier phase species volume fractions for cell, celli
const scalarField Xc(calcXc(celli));
// calculate mass transfer of each specie in liquid
forAll(activeLiquids_, i)
{
const label gid = liqToCarrierMap_[i];
const label lid = liqToLiqMap_[i];
// vapour diffusivity [m2/s]
const scalar Dab = liquids_.properties()[lid].D(pc, Ts);
// saturation pressure for species i [pa]
// - carrier phase pressure assumed equal to the liquid vapour pressure
// close to the surface
// NOTE: if pSat > pc then particle is superheated
// calculated evaporation rate will be greater than that of a particle
// at boiling point, but this is not a boiling model
const scalar pSat = liquids_.properties()[lid].pv(pc, T);
// Schmidt number
const scalar Sc = nu/(Dab + ROOTVSMALL);
// Sherwood number
const scalar Sh = this->Sh(Re, Sc);
// mass transfer coefficient [m/s]
const scalar kc = Sh*Dab/(d + ROOTVSMALL);
// vapour concentration at surface [kmol/m3] at film temperature
const scalar Cs = pSat/(RR*Ts);
// vapour concentration in bulk gas [kmol/m3] at bulk gas temperature
const scalar Cinf = Xc[gid]*pc/(RR*Tc);
// molar flux of vapour [kmol/m2/s]
const scalar Ni = max(kc*(Cs - Cinf), 0.0);
// droplet surface pressure assumed to surface vapour pressure
const scalar ps = liquids_.pv(pc, Ts, X);
// vapour density at droplet surface [kg/m3]
const scalar rhos = ps*liquids_.W(X)/(RR*Ts);
// vapour mass fraction at surface
const scalar Ys = min((Cs*liquids_.W(X)/rhos),0.9);
// vapour mass fraction in bulk gas
const scalar Yinf = Cinf*liquids_.W(X)/rhos;
// Spalding mass number
const scalar Bm = max(((Ys - Yinf)/(1.0 - Ys)),0.0);
// mass transfer [kg]
dMassPC[lid] += kc*pi*sqr(d)*rhoc*log(1+Bm)*dt;
}
}
template<class CloudType>
Foam::scalar Foam::LiquidEvaporationConvDiff<CloudType>::dh
(
const label idc,
const label idl,
const scalar p,
const scalar T
) const
{
scalar dh = 0;
typedef PhaseChangeModel<CloudType> parent;
switch (parent::enthalpyTransfer_)
{
case (parent::etLatentHeat):
{
dh = liquids_.properties()[idl].hl(p, T);
break;
}
case (parent::etEnthalpyDifference):
{
scalar hc = this->owner().composition().carrier().Ha(idc, p, T);
scalar hp = liquids_.properties()[idl].h(p, T);
dh = hc - hp;
break;
}
default:
{
FatalErrorInFunction
<< "Unknown enthalpyTransfer type" << abort(FatalError);
}
}
return dh;
}
template<class CloudType>
Foam::scalar Foam::LiquidEvaporationConvDiff<CloudType>::Tvap
(
const scalarField& X
) const
{
return liquids_.Tpt(X);
}
template<class CloudType>
Foam::scalar Foam::LiquidEvaporationConvDiff<CloudType>::TMax
(
const scalar p,
const scalarField& X
) const
{
return liquids_.pvInvert(p, X);
}
// ************************************************************************* //

View file

@ -0,0 +1,157 @@
/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | Copyright (C) 2011-2016 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
This file is part of OpenFOAM.
OpenFOAM is free software: you can redistribute it and/or modify it
under the terms of the GNU General Public License as published by
the Free Software Foundation, either version 3 of the License, or
(at your option) any later version.
OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License
for more details.
You should have received a copy of the GNU General Public License
along with OpenFOAM. If not, see <http://www.gnu.org/licenses/>.
Class
Foam::LiquidEvaporationConvDiff
Description
Liquid evaporation model
- uses ideal gas assumption
\*---------------------------------------------------------------------------*/
#ifndef LiquidEvaporationConvDiff_H
#define LiquidEvaporationConvDiff_H
#include "PhaseChangeModel.H"
#include "liquidMixtureProperties.H"
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
namespace Foam
{
/*---------------------------------------------------------------------------*\
Class LiquidEvaporationConvDiff Declaration
\*---------------------------------------------------------------------------*/
template<class CloudType>
class LiquidEvaporationConvDiff
:
public PhaseChangeModel<CloudType>
{
protected:
// Protected data
//- Global liquid properties data
const liquidMixtureProperties& liquids_;
//- List of active liquid names
List<word> activeLiquids_;
//- Mapping between liquid and carrier species
List<label> liqToCarrierMap_;
//- Mapping between local and global liquid species
List<label> liqToLiqMap_;
// Protected Member Functions
//- Sherwood number as a function of Reynolds and Schmidt numbers
scalar Sh(const scalar Re, const scalar Sc) const;
//- Calculate the carrier phase component volume fractions at celli
tmp<scalarField> calcXc(const label celli) const;
public:
//- Runtime type information
TypeName("liquidEvaporationConvDiff");
// Constructors
//- Construct from dictionary
LiquidEvaporationConvDiff(const dictionary& dict, CloudType& cloud);
//- Construct copy
LiquidEvaporationConvDiff(const LiquidEvaporationConvDiff<CloudType>& pcm);
//- Construct and return a clone
virtual autoPtr<PhaseChangeModel<CloudType>> clone() const
{
return autoPtr<PhaseChangeModel<CloudType>>
(
new LiquidEvaporationConvDiff<CloudType>(*this)
);
}
//- Destructor
virtual ~LiquidEvaporationConvDiff();
// Member Functions
//- Update model
virtual void calculate
(
const scalar dt,
const label celli,
const scalar Re,
const scalar Pr,
const scalar d,
const scalar nu,
const scalar T,
const scalar Ts,
const scalar pc,
const scalar Tc,
const scalarField& X,
scalarField& dMassPC,
const scalar rhoc
) const;
//- Return the enthalpy per unit mass
virtual scalar dh
(
const label idc,
const label idl,
const scalar p,
const scalar T
) const;
//- Return vapourisation temperature
virtual scalar Tvap(const scalarField& X) const;
//- Return maximum/limiting temperature
virtual scalar TMax(const scalar p, const scalarField& X) const;
};
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
} // End namespace Foam
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
#ifdef NoRepository
#include "LiquidEvaporationConvDiff.C"
#endif
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
#endif
// ************************************************************************* //

View file

@ -78,7 +78,8 @@ void Foam::NoPhaseChange<CloudType>::calculate
const scalar pc,
const scalar Tc,
const scalarField& X,
scalarField& dMassPC
scalarField& dMassPC,
const scalar rhoc
) const
{
// Nothing to do...

View file

@ -94,7 +94,8 @@ public:
const scalar pc,
const scalar Tc,
const scalarField& X,
scalarField& dMassPC
scalarField& dMassPC,
const scalar rhoc
) const;
};

View file

@ -166,7 +166,8 @@ public:
const scalar pc,
const scalar Tc,
const scalarField& X,
scalarField& dMassPC
scalarField& dMassPC,
const scalar rhoc
) const = 0;
//- Return the enthalpy per unit mass

View file

@ -148,7 +148,7 @@ irreversibleReactionDelimiter {space}"=>"{space}
startPDependentSpecie {space}"("{space}"+"{space}
pDependentSpecie {specieName}")"{space}
reactionCoeffs {space}{floatNum}{some_space}{floatNum}{some_space}{floatNum}{space}
reactionKeyword {space}[A-Za-z](([A-Za-z0-9)*-])|("("[^+]))*{space}
reactionKeyword {space}[A-Za-z](([A-Za-z0-9)*-])|("("[^+]))*((\+({some_space}))?){space}
reactionKeywordSlash {reactionKeyword}"/"{space}
thirdBodyEfficiency {space}{floatNum}{space}"/"{space}
startReactionCoeffs {space}"/"{space}
@ -637,7 +637,8 @@ bool finishReaction = false;
(
currentSpecieName,
1.0,
molecularWeight(currentSpecieComposition)
molecularWeight(currentSpecieComposition),
chargeNumber(currentSpecieComposition)
),
currentLowT,
currentHighT,

View file

@ -144,6 +144,28 @@ Foam::scalar Foam::chemkinReader::molecularWeight
}
Foam::scalar Foam::chemkinReader::chargeNumber
(
const List<specieElement>& specieComposition
) const
{
scalar nElemCharges = 0.0;
forAll(specieComposition, i)
{
label nAtoms = specieComposition[i].nAtoms;
const word& elementName = specieComposition[i].elementName;
if (elementName[0] == 'e')
{
nElemCharges -= nAtoms;
}
}
return nElemCharges;
}
void Foam::chemkinReader::checkCoeffs
(
const scalarList& reactionCoeffs,

View file

@ -254,6 +254,11 @@ private:
const List<specieElement>& specieComposition
) const;
scalar chargeNumber
(
const List<specieElement>& specieComposition
) const;
void finishElements(labelList& currentAtoms);
void checkCoeffs

View file

@ -68,6 +68,70 @@ Foam::scalar Foam::SpecieMixture<MixtureType>::W
}
template<class MixtureType>
Foam::scalar Foam::SpecieMixture<MixtureType>::z
(
const label speciei
) const
{
return this->getLocalThermo(speciei).z();
}
template<class MixtureType>
Foam::scalar Foam::SpecieMixture<MixtureType>::Qc
(
const label speciei
) const
{
return this->getLocalThermo(speciei).Qc();
}
template<class MixtureType>
Foam::scalar Foam::SpecieMixture<MixtureType>::Qc2
(
const label speciei
) const
{
return this->getLocalThermo(speciei).Qc2();
}
template<class MixtureType>
void Foam::SpecieMixture<MixtureType>::Cp
(
scalarField& Cps,
const scalar p,
const scalar T
) const
{
forAll(this->species(), speciei)
{
Cps[speciei] = this->getLocalThermo(speciei).Cp(p, T);
}
return;
}
template<class MixtureType>
void Foam::SpecieMixture<MixtureType>::Cv
(
scalarField& Cvs,
const scalar p,
const scalar T
) const
{
forAll(this->species(), speciei)
{
Cvs[speciei] = this->getLocalThermo(speciei).Cv(p, T);
}
return;
}
template<class MixtureType>
Foam::scalar Foam::SpecieMixture<MixtureType>::Cp
(

View file

@ -81,6 +81,34 @@ public:
//- Molecular weight of the given specie [kg/kmol]
virtual scalar W(const label speciei) const;
//- Number of charges of the given specie []
virtual scalar z(const label speciei) const;
//- Specific charge of the given specie []
virtual scalar Qc(const label specieI) const;
//- Absolute specific charge of the given specie []
virtual scalar Qc2(const label specieI) const;
// All species thermo properties
//- Heat capacity at constant pressure [J/(kg K)]
virtual void Cp
(
scalarField& Cps,
const scalar p,
const scalar T
) const;
//- Heat capacity at constant volume [J/(kg K)]
virtual void Cv
(
scalarField& Cvs,
const scalar p,
const scalar T
) const;
// Per specie thermo properties

View file

@ -81,4 +81,72 @@ Foam::tmp<Foam::volScalarField> Foam::basicSpecieMixture::W() const
}
Foam::tmp<Foam::volScalarField> Foam::basicSpecieMixture::Qc() const
{
const PtrList<volScalarField>& Y(basicMultiComponentMixture::Y());
tmp<volScalarField> tQc
(
new volScalarField
(
IOobject
(
IOobject::groupName("Qc", Y[0].group()),
Y[0].time().timeName(),
Y[0].mesh()
),
Y[0].mesh(),
dimensionedScalar("zero", dimCurrent*dimTime/dimMass, 0)
)
);
volScalarField& Qc = tQc.ref();
dimensionedScalar Qci("Qci", dimCurrent*dimTime/dimMass, 0);
forAll(Y, i)
{
Qci.value() = this->Qc(i);
Qc += Y[i]*Qci;
// Qc += Y[i]*this->Qc(i);
}
return tQc;
}
Foam::tmp<Foam::volScalarField> Foam::basicSpecieMixture::Qc2() const
{
const PtrList<volScalarField>& Y(basicMultiComponentMixture::Y());
tmp<volScalarField> tQc
(
new volScalarField
(
IOobject
(
IOobject::groupName("Qc2", Y[0].group()),
Y[0].time().timeName(),
Y[0].mesh()
),
Y[0].mesh(),
dimensionedScalar("zero", sqr(dimCurrent*dimTime)/dimMass, 0)
)
);
volScalarField& Qc = tQc.ref();
dimensionedScalar Qc2i("Qc2i", sqr(dimCurrent*dimTime)/dimMass, 0);
forAll(Y, i)
{
Qc2i.value() = this->Qc2(i);
Qc += Y[i]*Qc2i;
//Qc += Y[i]*this->Qc2(i);
}
return tQc;
}
// ************************************************************************* //

View file

@ -88,9 +88,43 @@ public:
//- Molecular weight of the given specie [kg/kmol]
virtual scalar W(const label speciei) const = 0;
//- Number of charges of the given specie []
virtual scalar z(const label speciei) const = 0;
//- Specific charge of the given specie [C/kg]
virtual scalar Qc(const label speciei) const = 0;
//- Absolute specific charge of the given specie [C/kg]
virtual scalar Qc2(const label speciei) const = 0;
//- Molecular weight of the mixture [kg/kmol]
tmp<volScalarField> W() const;
//- Specific charge of the mixture [C/kg]
tmp<volScalarField> Qc() const;
//- Absolute specific charge of the mixture [C^2/kg]
tmp<volScalarField> Qc2() const;
// All species thermo properties
//- Heat capacity at constant pressure [J/(kg K)]
virtual void Cp
(
scalarField& Cps,
const scalar p,
const scalar T
) const = 0;
//- Heat capacity at constant volume [J/(kg K)]
virtual void Cv
(
scalarField& Cvs,
const scalar p,
const scalar T
) const = 0;
// Per specie thermo properties

View file

@ -29,6 +29,24 @@ License
/* * * * * * * * * * * * * * * public constants * * * * * * * * * * * * * * */
//- Universal gas constant (default in [J/(kmol K)])
const Foam::scalar Foam::specie::RR = constant::physicoChemical::R.value()*1000;
//- Standard pressure (default in [Pa])
const Foam::scalar Foam::specie::Pstd = constant::standard::Pstd.value();
//- Standard temperature (default in [K])
const Foam::scalar Foam::specie::Tstd = constant::standard::Tstd.value();
//- Elementary charge (default in [C])
const Foam::scalar Foam::specie::e = constant::electromagnetic::e.value();
//- Avogadro number (default in [1/mol])
const Foam::scalar Foam::specie::NA = constant::physicoChemical::NA.value()*1000;
//- Boltzmann constant (default in [J/K])
const Foam::scalar Foam::specie::k = constant::physicoChemical::k.value();
namespace Foam
{
defineTypeNameAndDebug(specie, 0);
@ -41,7 +59,8 @@ Foam::specie::specie(Istream& is)
:
name_(is),
nMoles_(readScalar(is)),
molWeight_(readScalar(is))
molWeight_(readScalar(is)),
nCharges_(readScalar(is))
{
is.check("specie::specie(Istream& is)");
}
@ -51,7 +70,8 @@ Foam::specie::specie(const dictionary& dict)
:
name_(dict.dictName()),
nMoles_(readScalar(dict.subDict("specie").lookup("nMoles"))),
molWeight_(readScalar(dict.subDict("specie").lookup("molWeight")))
molWeight_(readScalar(dict.subDict("specie").lookup("molWeight"))),
nCharges_(dict.subDict("specie").lookupOrDefault("nCharges", 0.0))
{}
@ -62,6 +82,7 @@ void Foam::specie::write(Ostream& os) const
dictionary dict("specie");
dict.add("nMoles", nMoles_);
dict.add("molWeight", molWeight_);
dict.add("nCharges", nCharges_);
os << indent << dict.dictName() << dict;
}
@ -72,7 +93,8 @@ Foam::Ostream& Foam::operator<<(Ostream& os, const specie& st)
{
os << st.name_ << tab
<< st.nMoles_ << tab
<< st.molWeight_;
<< st.molWeight_ << tab
<< st.nCharges_;
os.check("Ostream& operator<<(Ostream& os, const specie& st)");
return os;

View file

@ -77,6 +77,9 @@ class specie
//- Molecular weight of specie [kg/kmol]
scalar molWeight_;
//- Number of elementary charges of specie
scalar nCharges_;
public:
@ -84,6 +87,29 @@ public:
ClassName("specie");
// Public constants
// Thermodynamic constants
//- Universal gas constant [J/(kmol K)]
static const scalar RR;
//- Standard pressure [Pa]
static const scalar Pstd;
//- Standard temperature [K]
static const scalar Tstd;
//- Elementary charge [C]
static const scalar e;
//- Avogadro number [1/kmol]
static const scalar NA;
//- Boltzmann constant [J/K]
static const scalar k;
// Constructors
@ -98,6 +124,23 @@ public:
const scalar molWeight
);
//- Construct from components without name
inline specie
(
const scalar nMoles,
const scalar molWeight,
const scalar nCharges
);
//- Construct from components with name
inline specie
(
const word& name,
const scalar nMoles,
const scalar molWeight,
const scalar nCharges
);
//- Construct as copy
inline specie(const specie&);
@ -127,6 +170,27 @@ public:
//- Gas constant [J/(kg K)]
inline scalar R() const;
//- Charge number
inline scalar z() const;
// Electric charge function
// Mole specific properties
//- Electric charge [C/kmol]
inline scalar qc() const;
// Mass specific properties
//- Electric charge [C/kg]
inline scalar Qc() const;
//- Electric charge squared [C^2/kg]
inline scalar Qc2() const;
// I-O

View file

@ -41,7 +41,8 @@ inline specie::specie
:
name_(name),
nMoles_(nMoles),
molWeight_(molWeight)
molWeight_(molWeight),
nCharges_(0.0)
{}
@ -52,7 +53,36 @@ inline specie::specie
)
:
nMoles_(nMoles),
molWeight_(molWeight)
molWeight_(molWeight),
nCharges_(0.0)
{}
inline specie::specie
(
const word& name,
const scalar nMoles,
const scalar molWeight,
const scalar nCharges
)
:
name_(name),
nMoles_(nMoles),
molWeight_(molWeight),
nCharges_(nCharges)
{}
inline specie::specie
(
const scalar nMoles,
const scalar molWeight,
const scalar nCharges
)
:
nMoles_(nMoles),
molWeight_(molWeight),
nCharges_(nCharges)
{}
@ -62,7 +92,8 @@ inline specie::specie(const specie& st)
:
name_(st.name_),
nMoles_(st.nMoles_),
molWeight_(st.molWeight_)
molWeight_(st.molWeight_),
nCharges_(st.nCharges_)
{}
@ -70,7 +101,8 @@ inline specie::specie(const word& name, const specie& st)
:
name_(name),
nMoles_(st.nMoles_),
molWeight_(st.molWeight_)
molWeight_(st.molWeight_),
nCharges_(st.nCharges_)
{}
@ -100,6 +132,30 @@ inline scalar specie::R() const
}
inline scalar specie::z() const
{
return nCharges_;
}
inline scalar specie::qc() const
{
return nCharges_ * NA * e;
}
inline scalar specie::Qc() const
{
return nCharges_ * NA * e / molWeight_;
}
inline scalar specie::Qc2() const
{
return nCharges_ * nCharges_ * NA * e * e / molWeight_;
}
// * * * * * * * * * * * * * * * Member Operators * * * * * * * * * * * * * //
inline void specie::operator=(const specie& st)
@ -107,6 +163,7 @@ inline void specie::operator=(const specie& st)
//name_ = st.name_;
nMoles_ = st.nMoles_;
molWeight_ = st.molWeight_;
nCharges_ = st.nCharges_;
}
@ -114,6 +171,10 @@ inline void specie::operator+=(const specie& st)
{
scalar sumNmoles = max(nMoles_ + st.nMoles_, SMALL);
nCharges_ =
nMoles_/sumNmoles*nCharges_
+ st.nMoles_/sumNmoles*st.nCharges_;
molWeight_ =
nMoles_/sumNmoles*molWeight_
+ st.nMoles_/sumNmoles*st.molWeight_;
@ -130,6 +191,10 @@ inline void specie::operator-=(const specie& st)
diffnMoles = SMALL;
}
nCharges_ =
nMoles_/diffnMoles*nCharges_
- st.nMoles_/diffnMoles*st.nCharges_;
molWeight_ =
nMoles_/diffnMoles*molWeight_
- st.nMoles_/diffnMoles*st.molWeight_;
@ -154,7 +219,9 @@ inline specie operator+(const specie& st1, const specie& st2)
(
sumNmoles,
st1.nMoles_/sumNmoles*st1.molWeight_
+ st2.nMoles_/sumNmoles*st2.molWeight_
+ st2.nMoles_/sumNmoles*st2.molWeight_,
st1.nMoles_/sumNmoles*st1.nCharges_
+ st2.nMoles_/sumNmoles*st2.nCharges_
);
}
@ -171,7 +238,9 @@ inline specie operator-(const specie& st1, const specie& st2)
(
diffNmoles,
st1.nMoles_/diffNmoles*st1.molWeight_
- st2.nMoles_/diffNmoles*st2.molWeight_
- st2.nMoles_/diffNmoles*st2.molWeight_,
st1.nMoles_/diffNmoles*st1.nCharges_
- st2.nMoles_/diffNmoles*st2.nCharges_
);
}
@ -181,7 +250,8 @@ inline specie operator*(const scalar s, const specie& st)
return specie
(
s*st.nMoles_,
st.molWeight_
st.molWeight_,
st.nCharges_
);
}

View file

@ -336,6 +336,7 @@ public:
) const;
// I-O
//- Write to Ostream