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https://develop.openfoam.com/Development/openfoam.git
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Merge branch 'master' of /home/noisy3/OpenFOAM/OpenFOAM-dev
This commit is contained in:
mattijs
@ -63,17 +63,28 @@ class OutputFilterFunctionObject
|
||||
{
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// Private data
|
||||
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||||
//- Output filter name
|
||||
word name_;
|
||||
|
||||
//- Reference to the time database
|
||||
const Time& time_;
|
||||
|
||||
//- Input dictionary
|
||||
dictionary dict_;
|
||||
|
||||
//- Name of region
|
||||
word regionName_;
|
||||
|
||||
//- Optional dictionary name to supply required inputs
|
||||
word dictName_;
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||||
|
||||
//- Switch for the execution of the functionObject
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bool enabled_;
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||||
|
||||
//- Output controls
|
||||
outputFilterOutputControl outputControl_;
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//- Pointer to the output filter
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autoPtr<OutputFilter> ptr_;
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@ -108,31 +119,78 @@ public:
|
||||
|
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// Member Functions
|
||||
|
||||
//- Return name
|
||||
virtual const word& name() const
|
||||
{
|
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return name_;
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||||
}
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// Access
|
||||
|
||||
//- Switch the function object on
|
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virtual void on();
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||||
//- Return name
|
||||
virtual const word& name() const
|
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{
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return name_;
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}
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//- Switch the function object off
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virtual void off();
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//- Return time database
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virtual const Time& time() const
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{
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return time_;
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}
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//- Return the input dictionary
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virtual const dictionary& dict() const
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{
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return dict_;
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}
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//- Return the region name
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virtual const word& regionName() const
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{
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return regionName_;
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}
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//- Return the optional dictionary name
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virtual const word& dictName() const
|
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{
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return dictName_;
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}
|
||||
|
||||
//- Return the enabled flag
|
||||
virtual bool enabled() const
|
||||
{
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return enabled_;
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}
|
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|
||||
//- Return the output control object
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virtual const outputFilterOutputControl& outputControl() const
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{
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return outputControl_;
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}
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//- Return the output filter
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virtual const OutputFilter& outputFilter() const
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{
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return ptr_();
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}
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//- Called at the start of the time-loop
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virtual bool start();
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// Function object control
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//- Called at each ++ or += of the time-loop
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virtual bool execute();
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//- Switch the function object on
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virtual void on();
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//- Called when Time::run() determines that the time-loop exits
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virtual bool end();
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//- Switch the function object off
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virtual void off();
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//- Read and set the function object if its data have changed
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virtual bool read(const dictionary&);
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//- Called at the start of the time-loop
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virtual bool start();
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//- Called at each ++ or += of the time-loop
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virtual bool execute();
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|
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//- Called when Time::run() determines that the time-loop exits
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virtual bool end();
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//- Read and set the function object if its data have changed
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virtual bool read(const dictionary&);
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};
|
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|
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@ -2,7 +2,7 @@
|
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========= |
|
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\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2008-2007 OpenCFD Ltd.
|
||||
\\ / A nd | Copyright (C) 2008-2009 OpenCFD Ltd.
|
||||
\\/ M anipulation |
|
||||
-------------------------------------------------------------------------------
|
||||
License
|
||||
|
||||
@ -2,7 +2,7 @@
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2008-2007 OpenCFD Ltd.
|
||||
\\ / A nd | Copyright (C) 2008-2009 OpenCFD Ltd.
|
||||
\\/ M anipulation |
|
||||
-------------------------------------------------------------------------------
|
||||
License
|
||||
|
||||
@ -2,7 +2,7 @@
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2008-2007 OpenCFD Ltd.
|
||||
\\ / A nd | Copyright (C) 2008-2009 OpenCFD Ltd.
|
||||
\\/ M anipulation |
|
||||
-------------------------------------------------------------------------------
|
||||
License
|
||||
|
||||
@ -2,7 +2,7 @@
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2008-2007 OpenCFD Ltd.
|
||||
\\ / A nd | Copyright (C) 2008-2009 OpenCFD Ltd.
|
||||
\\/ M anipulation |
|
||||
-------------------------------------------------------------------------------
|
||||
License
|
||||
|
||||
@ -2,7 +2,7 @@
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2008-2007 OpenCFD Ltd.
|
||||
\\ / A nd | Copyright (C) 2008-2009 OpenCFD Ltd.
|
||||
\\/ M anipulation |
|
||||
-------------------------------------------------------------------------------
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License
|
||||
|
||||
@ -299,7 +299,7 @@ void Foam::DsmcCloud<ParcelType>::collisions()
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// Temporary storage for subCells
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||||
List<DynamicList<label> > subCells(8);
|
||||
|
||||
scalar deltaT = mesh_.time().deltaT().value();
|
||||
scalar deltaT = cachedDeltaT();
|
||||
|
||||
label collisionCandidates = 0;
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||||
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||||
@ -778,6 +778,9 @@ Foam::DsmcCloud<ParcelType>::~DsmcCloud()
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||||
template<class ParcelType>
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void Foam::DsmcCloud<ParcelType>::evolve()
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{
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// cache the value of deltaT for this timestep
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storeDeltaT();
|
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|
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typename ParcelType::trackData td(*this);
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|
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// Reset the surface data collection fields
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||||
|
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@ -116,6 +116,10 @@ class DsmcCloud
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//- Random number generator
|
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Random rndGen_;
|
||||
|
||||
//- In-cloud cache of deltaT, lookup in submodels and parcel is
|
||||
// expensive
|
||||
scalar cachedDeltaT_;
|
||||
|
||||
|
||||
// References to the macroscopic fields
|
||||
|
||||
@ -243,6 +247,12 @@ public:
|
||||
//- Return refernce to the random object
|
||||
inline Random& rndGen();
|
||||
|
||||
//- Store (cache) the current value of deltaT
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||||
inline void storeDeltaT();
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||||
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||||
//- Return the cached value of deltaT
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inline scalar cachedDeltaT() const;
|
||||
|
||||
|
||||
// References to the surface data collection fields
|
||||
|
||||
|
||||
@ -120,6 +120,20 @@ inline Foam::Random& Foam::DsmcCloud<ParcelType>::rndGen()
|
||||
}
|
||||
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||||
|
||||
template<class ParcelType>
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inline void Foam::DsmcCloud<ParcelType>::storeDeltaT()
|
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{
|
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cachedDeltaT_ = mesh().time().deltaT().value();
|
||||
}
|
||||
|
||||
|
||||
template<class ParcelType>
|
||||
inline Foam::scalar Foam::DsmcCloud<ParcelType>::cachedDeltaT() const
|
||||
{
|
||||
return cachedDeltaT_;
|
||||
}
|
||||
|
||||
|
||||
template<class ParcelType>
|
||||
inline const Foam::volScalarField& Foam::DsmcCloud<ParcelType>::q() const
|
||||
{
|
||||
|
||||
@ -44,7 +44,7 @@ bool Foam::DsmcParcel<ParcelType>::move
|
||||
const polyMesh& mesh = td.cloud().pMesh();
|
||||
const polyBoundaryMesh& pbMesh = mesh.boundaryMesh();
|
||||
|
||||
const scalar deltaT = mesh.time().deltaT().value();
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const scalar deltaT = td.cloud().cachedDeltaT();
|
||||
scalar tEnd = (1.0 - p.stepFraction())*deltaT;
|
||||
const scalar dtMax = tEnd;
|
||||
|
||||
@ -145,7 +145,7 @@ void Foam::DsmcParcel<ParcelType>::hitWallPatch
|
||||
|
||||
const scalar fA = mag(wpp.faceAreas()[wppLocalFace]);
|
||||
|
||||
const scalar deltaT = td.cloud().mesh().time().deltaT().value();
|
||||
const scalar deltaT = td.cloud().cachedDeltaT();
|
||||
|
||||
scalar deltaQ = td.cloud().nParticle()*(preIE - postIE)/(deltaT*fA);
|
||||
|
||||
|
||||
@ -126,7 +126,7 @@ void Foam::FreeStream<CloudType>::inflow()
|
||||
|
||||
const polyMesh& mesh(cloud.mesh());
|
||||
|
||||
const scalar deltaT = mesh.time().deltaT().value();
|
||||
const scalar deltaT = cloud.cachedDeltaT();
|
||||
|
||||
Random& rndGen(cloud.rndGen());
|
||||
|
||||
|
||||
@ -177,6 +177,7 @@ template<class ParcelType>
|
||||
void Foam::KinematicCloud<ParcelType>::preEvolve()
|
||||
{
|
||||
this->dispersion().cacheFields(true);
|
||||
forces_.cacheFields(true);
|
||||
}
|
||||
|
||||
|
||||
@ -189,6 +190,7 @@ void Foam::KinematicCloud<ParcelType>::postEvolve()
|
||||
}
|
||||
|
||||
this->dispersion().cacheFields(false);
|
||||
forces_.cacheFields(false);
|
||||
|
||||
this->postProcessing().post();
|
||||
}
|
||||
|
||||
@ -274,18 +274,6 @@ public:
|
||||
inline const dictionary& interpolationSchemes() const;
|
||||
|
||||
|
||||
// Forces to include in particle motion evaluation
|
||||
|
||||
//- Return reference to the gravity force flag
|
||||
inline Switch forceGravity() const;
|
||||
|
||||
//- Return reference to the virtual mass force flag
|
||||
inline Switch forceVirtualMass() const;
|
||||
|
||||
//- Return reference to the pressure gradient force flag
|
||||
inline Switch forcePressureGradient() const;
|
||||
|
||||
|
||||
// Sub-models
|
||||
|
||||
//- Return const-access to the dispersion model
|
||||
|
||||
@ -27,6 +27,7 @@ License
|
||||
#include "particleForces.H"
|
||||
#include "fvMesh.H"
|
||||
#include "volFields.H"
|
||||
#include "fvcGrad.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
@ -40,21 +41,17 @@ Foam::particleForces::particleForces
|
||||
mesh_(mesh),
|
||||
dict_(dict.subDict("particleForces")),
|
||||
g_(g),
|
||||
gradUPtr_(NULL),
|
||||
gravity_(dict_.lookup("gravity")),
|
||||
virtualMass_(dict_.lookup("virtualMass")),
|
||||
Cvm_(0.0),
|
||||
pressureGradient_(dict_.lookup("pressureGradient")),
|
||||
gradUName_("unknown_gradUName")
|
||||
UName_(dict_.lookupOrDefault<word>("U", "U"))
|
||||
{
|
||||
if (gravity_)
|
||||
if (virtualMass_)
|
||||
{
|
||||
dict_.lookup("Cvm") >> Cvm_;
|
||||
}
|
||||
|
||||
if (pressureGradient_)
|
||||
{
|
||||
dict_.lookup("gradU") >> gradUName_;
|
||||
}
|
||||
}
|
||||
|
||||
|
||||
@ -63,18 +60,21 @@ Foam::particleForces::particleForces(const particleForces& f)
|
||||
mesh_(f.mesh_),
|
||||
dict_(f.dict_),
|
||||
g_(f.g_),
|
||||
gradUPtr_(f.gradUPtr_),
|
||||
gravity_(f.gravity_),
|
||||
virtualMass_(f.virtualMass_),
|
||||
Cvm_(f.Cvm_),
|
||||
pressureGradient_(f.pressureGradient_),
|
||||
gradUName_(f.gradUName_)
|
||||
UName_(f.UName_)
|
||||
{}
|
||||
|
||||
|
||||
// * * * * * * * * * * * * * * * * Destructor * * * * * * * * * * * * * * * //
|
||||
|
||||
Foam::particleForces::~particleForces()
|
||||
{}
|
||||
{
|
||||
cacheFields(false);
|
||||
}
|
||||
|
||||
|
||||
// * * * * * * * * * * * * * * * Member Functions * * * * * * * * * * * * * //
|
||||
@ -109,9 +109,26 @@ Foam::Switch Foam::particleForces::pressureGradient() const
|
||||
}
|
||||
|
||||
|
||||
const Foam::word& Foam::particleForces::gradUName() const
|
||||
const Foam::word& Foam::particleForces::UName() const
|
||||
{
|
||||
return gradUName_;
|
||||
return UName_;
|
||||
}
|
||||
|
||||
|
||||
void Foam::particleForces::cacheFields(const bool store)
|
||||
{
|
||||
if (store && pressureGradient_)
|
||||
{
|
||||
const volVectorField U = mesh_.lookupObject<volVectorField>(UName_);
|
||||
gradUPtr_ = fvc::grad(U).ptr();
|
||||
}
|
||||
else
|
||||
{
|
||||
if (gradUPtr_)
|
||||
{
|
||||
delete gradUPtr_;
|
||||
}
|
||||
}
|
||||
}
|
||||
|
||||
|
||||
@ -130,15 +147,17 @@ Foam::vector Foam::particleForces::calcCoupled
|
||||
// Virtual mass force
|
||||
if (virtualMass_)
|
||||
{
|
||||
notImplemented("Foam::particleForces::calc(...) - virtualMass force");
|
||||
notImplemented
|
||||
(
|
||||
"Foam::particleForces::calcCoupled(...) - virtual mass force"
|
||||
);
|
||||
// Ftot += Cvm_*rhoc/rho*d(Uc - U)/dt;
|
||||
}
|
||||
|
||||
// Pressure gradient force
|
||||
if (pressureGradient_)
|
||||
{
|
||||
const volSymmTensorField& gradU =
|
||||
mesh_.lookupObject<volSymmTensorField>(gradUName_);
|
||||
const volTensorField& gradU = *gradUPtr_;
|
||||
Ftot += rhoc/rho*(U & gradU[cellI]);
|
||||
}
|
||||
|
||||
|
||||
@ -39,6 +39,7 @@ SourceFiles
|
||||
#include "dictionary.H"
|
||||
#include "Switch.H"
|
||||
#include "vector.H"
|
||||
#include "volFieldsFwd.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
@ -65,6 +66,9 @@ class particleForces
|
||||
//- Gravity
|
||||
const vector g_;
|
||||
|
||||
//- Velocity gradient field
|
||||
const volTensorField* gradUPtr_;
|
||||
|
||||
|
||||
// Forces to include in particle motion evaluation
|
||||
|
||||
@ -80,8 +84,11 @@ class particleForces
|
||||
//- Pressure gradient
|
||||
Switch pressureGradient_;
|
||||
|
||||
//- Name of velocity gradient field for pressure gradient force
|
||||
word gradUName_;
|
||||
|
||||
// Additional info
|
||||
|
||||
//- Name of velucity field - default = "U"
|
||||
const word UName_;
|
||||
|
||||
|
||||
public:
|
||||
@ -126,12 +133,15 @@ public:
|
||||
//- Return pressure gradient force activate switch
|
||||
Switch pressureGradient() const;
|
||||
|
||||
//- Return the name of the velocity gradient field
|
||||
const word& gradUName() const;
|
||||
//- Return name of velocity field
|
||||
const word& UName() const;
|
||||
|
||||
|
||||
// Evaluation
|
||||
|
||||
//- Cache carrier fields
|
||||
void cacheFields(const bool store);
|
||||
|
||||
//- Calculate action/reaction forces between carrier and particles
|
||||
vector calcCoupled
|
||||
(
|
||||
|
||||
@ -507,7 +507,7 @@ void Foam::moleculeCloud::initialiseMolecules
|
||||
else
|
||||
{
|
||||
const dictionary& zoneDict =
|
||||
mdInitialiseDict.subDict(zone.name());
|
||||
mdInitialiseDict.subDict(zone.name());
|
||||
|
||||
const scalar temperature
|
||||
(
|
||||
@ -530,7 +530,7 @@ void Foam::moleculeCloud::initialiseMolecules
|
||||
{
|
||||
FatalErrorIn("Foam::moleculeCloud::initialiseMolecules")
|
||||
<< "latticeIds and latticePositions must be the same "
|
||||
<< " size." << nl
|
||||
<< " size." << nl
|
||||
<< abort(FatalError);
|
||||
}
|
||||
|
||||
@ -548,6 +548,15 @@ void Foam::moleculeCloud::initialiseMolecules
|
||||
zoneDict.lookup("numberDensity")
|
||||
);
|
||||
|
||||
if (numberDensity < VSMALL)
|
||||
{
|
||||
WarningIn("moleculeCloud::initialiseMolecules")
|
||||
<< "numberDensity too small, not filling zone "
|
||||
<< zone.name() << endl;
|
||||
|
||||
continue;
|
||||
}
|
||||
|
||||
latticeCellScale = pow
|
||||
(
|
||||
latticeIds.size()/(det(latticeCellShape)*numberDensity),
|
||||
@ -572,9 +581,19 @@ void Foam::moleculeCloud::initialiseMolecules
|
||||
zoneDict.lookup("massDensity")
|
||||
);
|
||||
|
||||
if (massDensity < VSMALL)
|
||||
{
|
||||
WarningIn("moleculeCloud::initialiseMolecules")
|
||||
<< "massDensity too small, not filling zone "
|
||||
<< zone.name() << endl;
|
||||
|
||||
continue;
|
||||
}
|
||||
|
||||
|
||||
latticeCellScale = pow
|
||||
(
|
||||
unitCellMass /(det(latticeCellShape)*massDensity),
|
||||
unitCellMass/(det(latticeCellShape)*massDensity),
|
||||
(1.0/3.0)
|
||||
);
|
||||
}
|
||||
@ -906,7 +925,7 @@ void Foam::moleculeCloud::initialiseMolecules
|
||||
)
|
||||
{
|
||||
WarningIn("Foam::moleculeCloud::initialiseMolecules()")
|
||||
<< "A whole layer of unit cells was placed "
|
||||
<< "A whole layer of unit cells was placed "
|
||||
<< "outside the bounds of the mesh, but no "
|
||||
<< "molecules have been placed in zone '"
|
||||
<< zone.name()
|
||||
|
||||
@ -127,11 +127,11 @@ void Foam::staticPressure::write()
|
||||
{
|
||||
const volScalarField& p = obr_.lookupObject<volScalarField>(pName_);
|
||||
|
||||
volScalarField pDyn
|
||||
volScalarField pStatic
|
||||
(
|
||||
IOobject
|
||||
(
|
||||
"pDyn",
|
||||
"pStatic",
|
||||
obr_.time().timeName(),
|
||||
obr_,
|
||||
IOobject::NO_READ
|
||||
@ -139,7 +139,7 @@ void Foam::staticPressure::write()
|
||||
dimensionedScalar("rho", dimDensity, rho_)*p
|
||||
);
|
||||
|
||||
pDyn.write();
|
||||
pStatic.write();
|
||||
}
|
||||
}
|
||||
|
||||
|
||||
4
src/postProcessing/functionObjects/zones/Make/files
Normal file
4
src/postProcessing/functionObjects/zones/Make/files
Normal file
@ -0,0 +1,4 @@
|
||||
faceZoneIntegration/faceZonesIntegration.C
|
||||
faceZoneIntegration/faceZonesIntegrationFunctionObject.C
|
||||
|
||||
LIB = $(FOAM_LIBBIN)/libzoneFunctionObjects
|
||||
9
src/postProcessing/functionObjects/zones/Make/options
Normal file
9
src/postProcessing/functionObjects/zones/Make/options
Normal file
@ -0,0 +1,9 @@
|
||||
EXE_INC = \
|
||||
-I$(LIB_SRC)/finiteVolume/lnInclude \
|
||||
-I$(LIB_SRC)/meshTools/lnInclude \
|
||||
-I$(LIB_SRC)/sampling/lnInclude
|
||||
|
||||
LIB_LIBS = \
|
||||
-lfiniteVolume \
|
||||
-lmeshTools \
|
||||
-lsampling
|
||||
@ -0,0 +1,50 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2009-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
Typedef
|
||||
Foam::IOfaceZonesIntegration
|
||||
|
||||
Description
|
||||
Instance of the generic IOOutputFilter for faceZonesIntegration.
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
#ifndef IOfaceZonesIntegration_H
|
||||
#define IOfaceZonesIntegration_H
|
||||
|
||||
#include "faceZonesIntegration.H"
|
||||
#include "IOOutputFilter.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
typedef IOOutputFilter<faceZonesIntegration> IOfaceZonesIntegration;
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -0,0 +1,322 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2009-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
#include "faceZonesIntegration.H"
|
||||
#include "volFields.H"
|
||||
#include "dictionary.H"
|
||||
#include "Time.H"
|
||||
#include "IOmanip.H"
|
||||
#include "ListListOps.H"
|
||||
#include "processorPolyPatch.H"
|
||||
#include "cyclicPolyPatch.H"
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(faceZonesIntegration, 0);
|
||||
}
|
||||
|
||||
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
Foam::faceZonesIntegration::faceZonesIntegration
|
||||
(
|
||||
const word& name,
|
||||
const objectRegistry& obr,
|
||||
const dictionary& dict,
|
||||
const bool loadFromFiles
|
||||
)
|
||||
:
|
||||
name_(name),
|
||||
obr_(obr),
|
||||
active_(true),
|
||||
log_(false),
|
||||
faceZonesSet_(),
|
||||
fItems_(),
|
||||
faceZonesIntegrationFilePtr_(NULL)
|
||||
{
|
||||
// Check if the available mesh is an fvMesh otherise deactivate
|
||||
if (!isA<fvMesh>(obr_))
|
||||
{
|
||||
active_ = false;
|
||||
WarningIn
|
||||
(
|
||||
"Foam::faceZonesIntegration::faceZonesIntegration"
|
||||
"("
|
||||
"const word&, "
|
||||
"const objectRegistry&, "
|
||||
"const dictionary&, "
|
||||
"const bool"
|
||||
")"
|
||||
) << "No fvMesh available, deactivating."
|
||||
<< endl;
|
||||
}
|
||||
|
||||
read(dict);
|
||||
}
|
||||
|
||||
|
||||
// * * * * * * * * * * * * * * * * Destructor * * * * * * * * * * * * * * * //
|
||||
|
||||
Foam::faceZonesIntegration::~faceZonesIntegration()
|
||||
{}
|
||||
|
||||
|
||||
// * * * * * * * * * * * * * * * Member Functions * * * * * * * * * * * * * //
|
||||
|
||||
void Foam::faceZonesIntegration::read(const dictionary& dict)
|
||||
{
|
||||
if (active_)
|
||||
{
|
||||
log_ = dict.lookupOrDefault<Switch>("log", false);
|
||||
|
||||
dict.lookup("fields") >> fItems_;
|
||||
|
||||
dict.lookup("faceZones") >> faceZonesSet_;
|
||||
}
|
||||
}
|
||||
|
||||
|
||||
void Foam::faceZonesIntegration::makeFile()
|
||||
{
|
||||
// Create the face Zone file if not already created
|
||||
if (faceZonesIntegrationFilePtr_.empty())
|
||||
{
|
||||
if (debug)
|
||||
{
|
||||
Info<< "Creating faceZonesIntegration file." << endl;
|
||||
}
|
||||
|
||||
// File update
|
||||
if (Pstream::master())
|
||||
{
|
||||
fileName faceZonesIntegrationDir;
|
||||
if (Pstream::parRun())
|
||||
{
|
||||
// Put in undecomposed case (Note: gives problems for
|
||||
// distributed data running)
|
||||
faceZonesIntegrationDir =
|
||||
obr_.time().path()/".."/name_/obr_.time().timeName();
|
||||
}
|
||||
else
|
||||
{
|
||||
faceZonesIntegrationDir =
|
||||
obr_.time().path()/name_/obr_.time().timeName();
|
||||
}
|
||||
|
||||
// Create directory if does not exist.
|
||||
mkDir(faceZonesIntegrationDir);
|
||||
|
||||
// Open new file at start up
|
||||
faceZonesIntegrationFilePtr_.resize(fItems_.size());
|
||||
|
||||
forAll(fItems_, Ifields)
|
||||
{
|
||||
const word& fieldName = fItems_[Ifields];
|
||||
|
||||
OFstream* sPtr = new OFstream
|
||||
(
|
||||
faceZonesIntegrationDir/fieldName
|
||||
);
|
||||
|
||||
faceZonesIntegrationFilePtr_.insert(fieldName, sPtr);
|
||||
}
|
||||
|
||||
// Add headers to output data
|
||||
writeFileHeader();
|
||||
}
|
||||
}
|
||||
}
|
||||
|
||||
|
||||
void Foam::faceZonesIntegration::writeFileHeader()
|
||||
{
|
||||
forAllIter(HashPtrTable<OFstream>, faceZonesIntegrationFilePtr_, iter)
|
||||
{
|
||||
unsigned int w = IOstream::defaultPrecision() + 7;
|
||||
|
||||
OFstream& os = *faceZonesIntegrationFilePtr_[iter.key()];
|
||||
|
||||
os << "#Time " << setw(w);
|
||||
|
||||
forAll (faceZonesSet_, zoneI)
|
||||
{
|
||||
const word name = faceZonesSet_[zoneI];
|
||||
os << name << setw(w);
|
||||
}
|
||||
|
||||
os << nl << endl;
|
||||
}
|
||||
}
|
||||
|
||||
|
||||
void Foam::faceZonesIntegration::execute()
|
||||
{
|
||||
// Do nothing - only valid on write
|
||||
}
|
||||
|
||||
|
||||
void Foam::faceZonesIntegration::end()
|
||||
{
|
||||
// Do nothing - only valid on write
|
||||
}
|
||||
|
||||
|
||||
void Foam::faceZonesIntegration::write()
|
||||
{
|
||||
if (active_)
|
||||
{
|
||||
makeFile();
|
||||
scalar dm = 0.0;
|
||||
forAll(fItems_, fieldI)
|
||||
{
|
||||
const word& fieldName = fItems_[fieldI];
|
||||
|
||||
const surfaceScalarField& fD =
|
||||
obr_.lookupObject<surfaceScalarField>(fieldName);
|
||||
|
||||
const fvMesh& mesh = fD.mesh();
|
||||
|
||||
unsigned int w = IOstream::defaultPrecision() + 7;
|
||||
|
||||
if
|
||||
(
|
||||
Pstream::master()
|
||||
&& faceZonesIntegrationFilePtr_.found(fieldName)
|
||||
)
|
||||
{
|
||||
OFstream& os = *faceZonesIntegrationFilePtr_(fieldName);
|
||||
|
||||
os << obr_.time().value();
|
||||
|
||||
const faceZoneMesh& faceZoneList = mesh.faceZones();
|
||||
|
||||
forAll(faceZonesSet_, zoneI)
|
||||
{
|
||||
const word name = faceZonesSet_[zoneI];
|
||||
|
||||
label zoneID = faceZoneList.findZoneID(name);
|
||||
|
||||
const faceZone& fz = mesh.faceZones()[zoneID];
|
||||
|
||||
dm = calcFaceZonesIntegral(fD, fz);
|
||||
|
||||
reduce(dm, sumOp<scalar>());
|
||||
|
||||
os << ' ' << setw(w) << dm;
|
||||
|
||||
if (log_)
|
||||
{
|
||||
Info<< "faceZonesIntegration output:" << nl
|
||||
<< " Integration" << dm << endl;
|
||||
}
|
||||
}
|
||||
|
||||
os << endl;
|
||||
}
|
||||
}
|
||||
}
|
||||
}
|
||||
|
||||
|
||||
Foam::scalar Foam::faceZonesIntegration::calcFaceZonesIntegral
|
||||
(
|
||||
const surfaceScalarField& fD,
|
||||
const faceZone& fz
|
||||
) const
|
||||
{
|
||||
scalar dm = 0.0;
|
||||
const fvMesh& mesh = fD.mesh();
|
||||
|
||||
forAll (fz, i)
|
||||
{
|
||||
label faceI = fz[i];
|
||||
|
||||
if (mesh.isInternalFace(faceI))
|
||||
{
|
||||
if (fz.flipMap()[faceI])
|
||||
{
|
||||
dm -= fD[faceI];
|
||||
}
|
||||
else
|
||||
{
|
||||
dm += fD[faceI];
|
||||
}
|
||||
}
|
||||
else
|
||||
{
|
||||
label patchI = mesh.boundaryMesh().whichPatch(faceI);
|
||||
const polyPatch& pp = mesh.boundaryMesh()[patchI];
|
||||
if (isA<processorPolyPatch>(pp))
|
||||
{
|
||||
if (refCast<const processorPolyPatch>(pp).owner())
|
||||
{
|
||||
if (fz.flipMap()[faceI])
|
||||
{
|
||||
dm -= fD.boundaryField()[patchI][pp.whichFace(faceI)];
|
||||
}
|
||||
else
|
||||
{
|
||||
dm += fD.boundaryField()[patchI][pp.whichFace(faceI)];
|
||||
}
|
||||
}
|
||||
}
|
||||
else if (isA<cyclicPolyPatch>(pp))
|
||||
{
|
||||
label patchFaceI = faceI - pp.start();
|
||||
if (patchFaceI < pp.size()/2)
|
||||
{
|
||||
if (fz.flipMap()[patchFaceI])
|
||||
{
|
||||
dm -= fD.boundaryField()[patchI][patchFaceI];
|
||||
}
|
||||
else
|
||||
{
|
||||
dm += fD.boundaryField()[patchI][patchFaceI];
|
||||
}
|
||||
}
|
||||
}
|
||||
else if (!isA<emptyPolyPatch>(pp))
|
||||
{
|
||||
label patchFaceI = faceI - pp.start();
|
||||
if (fz.flipMap()[patchFaceI])
|
||||
{
|
||||
dm -= fD.boundaryField()[patchI][patchFaceI];
|
||||
}
|
||||
else
|
||||
{
|
||||
dm += fD.boundaryField()[patchI][patchFaceI];
|
||||
}
|
||||
}
|
||||
}
|
||||
}
|
||||
|
||||
return dm;
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -0,0 +1,178 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2009-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
Class
|
||||
Foam::faceZonesIntegration
|
||||
|
||||
Description
|
||||
Integrates surfaceScalarFields on faceZones
|
||||
|
||||
SourceFiles
|
||||
faceZonesIntegration.C
|
||||
IOfaceZonesIntegration.H
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
#ifndef faceZonesIntegration_H
|
||||
#define faceZonesIntegration_H
|
||||
|
||||
#include "fvCFD.H"
|
||||
#include "primitiveFieldsFwd.H"
|
||||
#include "volFieldsFwd.H"
|
||||
#include "HashPtrTable.H"
|
||||
#include "OFstream.H"
|
||||
#include "Switch.H"
|
||||
#include "pointFieldFwd.H"
|
||||
#include "polyMesh.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
|
||||
// Forward declaration of classes
|
||||
class objectRegistry;
|
||||
class dictionary;
|
||||
class mapPolyMesh;
|
||||
|
||||
/*---------------------------------------------------------------------------*\
|
||||
Class faceZonesIntegration Declaration
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
class faceZonesIntegration
|
||||
{
|
||||
|
||||
protected:
|
||||
|
||||
// Private data
|
||||
|
||||
//- Name of this set of face zone integration,
|
||||
// Also used as the name of the probes directory.
|
||||
word name_;
|
||||
|
||||
const objectRegistry& obr_;
|
||||
|
||||
//- on/off switch
|
||||
bool active_;
|
||||
|
||||
//- Switch to send output to Info as well as to file
|
||||
Switch log_;
|
||||
|
||||
//- Current open files
|
||||
HashPtrTable<OFstream> faceZonesIntegrationFilePtr_;
|
||||
|
||||
// Read from dictionary
|
||||
|
||||
//- faceZones to integrate over
|
||||
wordList faceZonesSet_;
|
||||
|
||||
//- Names of the surface fields
|
||||
wordList fItems_;
|
||||
|
||||
|
||||
// Private Member Functions
|
||||
|
||||
//- If the integration file has not been created create it
|
||||
void makeFile();
|
||||
|
||||
scalar calcFaceZonesIntegral
|
||||
(
|
||||
const surfaceScalarField& fD,
|
||||
const faceZone& fz
|
||||
) const;
|
||||
|
||||
|
||||
//- Disallow default bitwise copy construct
|
||||
faceZonesIntegration(const faceZonesIntegration&);
|
||||
|
||||
//- Disallow default bitwise assignment
|
||||
void operator=(const faceZonesIntegration&);
|
||||
|
||||
//- Output file header information
|
||||
virtual void writeFileHeader();
|
||||
|
||||
|
||||
public:
|
||||
|
||||
//- Runtime type information
|
||||
TypeName("faceZonesIntegration");
|
||||
|
||||
|
||||
// Constructors
|
||||
|
||||
//- Construct for given objectRegistry and dictionary.
|
||||
// Allow the possibility to load fields from files
|
||||
faceZonesIntegration
|
||||
(
|
||||
const word& name,
|
||||
const objectRegistry&,
|
||||
const dictionary&,
|
||||
const bool loadFromFiles = false
|
||||
);
|
||||
|
||||
|
||||
// Destructor
|
||||
|
||||
virtual ~faceZonesIntegration();
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Return name of the set of zones
|
||||
virtual const word& name() const
|
||||
{
|
||||
return name_;
|
||||
};
|
||||
|
||||
//- Read the zone integration data
|
||||
virtual void read(const dictionary&);
|
||||
|
||||
//- Execute, currently does nothing
|
||||
virtual void execute();
|
||||
|
||||
//- Execute at the final time-loop, currently does nothing
|
||||
virtual void end();
|
||||
|
||||
//- Write the integration
|
||||
virtual void write();
|
||||
|
||||
//- Update for changes of mesh
|
||||
virtual void updateMesh(const mapPolyMesh&)
|
||||
{}
|
||||
|
||||
//- Update for changes of mesh
|
||||
virtual void movePoints(const pointField&)
|
||||
{}
|
||||
};
|
||||
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -0,0 +1,43 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2009-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
#include "faceZonesIntegrationFunctionObject.H"
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineNamedTemplateTypeNameAndDebug(faceZonesIntegrationFunctionObject, 0);
|
||||
|
||||
addToRunTimeSelectionTable
|
||||
(
|
||||
functionObject,
|
||||
faceZonesIntegrationFunctionObject,
|
||||
dictionary
|
||||
);
|
||||
}
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -0,0 +1,55 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2009-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
Typedef
|
||||
Foam::faceZonesIntegrationFunctionObject
|
||||
|
||||
Description
|
||||
FunctionObject wrapper around faceZonesIntegration to allow them to be
|
||||
created via the functions list within controlDict.
|
||||
|
||||
SourceFiles
|
||||
faceZonesIntegrationFunctionObject.C
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
#ifndef faceZonesIntegrationFunctionObject_H
|
||||
#define faceZonesIntegrationFunctionObject_H
|
||||
|
||||
#include "faceZonesIntegration.H"
|
||||
#include "OutputFilterFunctionObject.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
typedef OutputFilterFunctionObject<faceZonesIntegration>
|
||||
faceZonesIntegrationFunctionObject;
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -175,9 +175,8 @@ public:
|
||||
);
|
||||
|
||||
|
||||
// Destructor
|
||||
|
||||
virtual ~probes();
|
||||
//- Destructor
|
||||
virtual ~probes();
|
||||
|
||||
|
||||
// Member Functions
|
||||
@ -188,6 +187,18 @@ public:
|
||||
return name_;
|
||||
}
|
||||
|
||||
//- Return names of fields to probe
|
||||
virtual const wordList& fieldNames() const
|
||||
{
|
||||
return fieldNames_;
|
||||
}
|
||||
|
||||
//- Return locations to probe
|
||||
virtual const vectorField& probeLocations() const
|
||||
{
|
||||
return probeLocations_;
|
||||
}
|
||||
|
||||
//- Cells to be probed (obtained from the locations)
|
||||
const labelList& cells() const
|
||||
{
|
||||
|
||||
@ -34,7 +34,6 @@ const Foam::scalar Foam::liquidMixture::TrMax = 0.999;
|
||||
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
// Construct from components
|
||||
Foam::liquidMixture::liquidMixture
|
||||
(
|
||||
const dictionary& thermophysicalProperties
|
||||
@ -72,6 +71,7 @@ Foam::liquidMixture::liquidMixture
|
||||
}
|
||||
}
|
||||
|
||||
|
||||
// * * * * * * * * * * * * * * * * Selectors * * * * * * * * * * * * * * * * //
|
||||
|
||||
Foam::autoPtr<Foam::liquidMixture> Foam::liquidMixture::New
|
||||
@ -85,7 +85,6 @@ Foam::autoPtr<Foam::liquidMixture> Foam::liquidMixture::New
|
||||
|
||||
// * * * * * * * * * * * * * * * Member Functions * * * * * * * * * * * * * //
|
||||
|
||||
// Critical Temperature
|
||||
Foam::scalar Foam::liquidMixture::Tc
|
||||
(
|
||||
const scalarField& x
|
||||
@ -104,9 +103,8 @@ Foam::scalar Foam::liquidMixture::Tc
|
||||
|
||||
return vTc/vc;
|
||||
}
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
// Pseudocritical temperature
|
||||
|
||||
Foam::scalar Foam::liquidMixture::Tpc
|
||||
(
|
||||
const scalarField& x
|
||||
@ -121,9 +119,7 @@ Foam::scalar Foam::liquidMixture::Tpc
|
||||
return Tpc;
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
// Pseudocritical pressure
|
||||
Foam::scalar Foam::liquidMixture::Ppc
|
||||
(
|
||||
const scalarField& x
|
||||
@ -140,7 +136,6 @@ Foam::scalar Foam::liquidMixture::Ppc
|
||||
return specie::RR*Zc*Tpc(x)/Vc;
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
Foam::scalar Foam::liquidMixture::omega
|
||||
(
|
||||
@ -156,7 +151,6 @@ Foam::scalar Foam::liquidMixture::omega
|
||||
return omega;
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
Foam::scalarField Foam::liquidMixture::Xs
|
||||
(
|
||||
@ -178,9 +172,6 @@ Foam::scalarField Foam::liquidMixture::Xs
|
||||
return xs;
|
||||
}
|
||||
|
||||
//-----------------------------------------------------------------------------
|
||||
// Physical properties
|
||||
//-----------------------------------------------------------------------------
|
||||
|
||||
Foam::scalar Foam::liquidMixture::W
|
||||
(
|
||||
@ -196,6 +187,7 @@ Foam::scalar Foam::liquidMixture::W
|
||||
return W;
|
||||
}
|
||||
|
||||
|
||||
Foam::scalarField Foam::liquidMixture::Y
|
||||
(
|
||||
const scalarField& X
|
||||
@ -211,6 +203,7 @@ Foam::scalarField Foam::liquidMixture::Y
|
||||
return Y;
|
||||
}
|
||||
|
||||
|
||||
Foam::scalarField Foam::liquidMixture::X
|
||||
(
|
||||
const scalarField& Y
|
||||
@ -250,6 +243,7 @@ Foam::scalar Foam::liquidMixture::rho
|
||||
return W(x)/v;
|
||||
}
|
||||
|
||||
|
||||
Foam::scalar Foam::liquidMixture::pv
|
||||
(
|
||||
const scalar p,
|
||||
@ -271,6 +265,7 @@ Foam::scalar Foam::liquidMixture::pv
|
||||
return pv/W(x);
|
||||
}
|
||||
|
||||
|
||||
Foam::scalar Foam::liquidMixture::hl
|
||||
(
|
||||
const scalar p,
|
||||
@ -292,6 +287,7 @@ Foam::scalar Foam::liquidMixture::hl
|
||||
return hl/W(x);
|
||||
}
|
||||
|
||||
|
||||
Foam::scalar Foam::liquidMixture::cp
|
||||
(
|
||||
const scalar p,
|
||||
@ -313,6 +309,7 @@ Foam::scalar Foam::liquidMixture::cp
|
||||
return cp/W(x);
|
||||
}
|
||||
|
||||
|
||||
Foam::scalar Foam::liquidMixture::sigma
|
||||
(
|
||||
const scalar p,
|
||||
@ -346,6 +343,7 @@ Foam::scalar Foam::liquidMixture::sigma
|
||||
return sigma;
|
||||
}
|
||||
|
||||
|
||||
Foam::scalar Foam::liquidMixture::mu
|
||||
(
|
||||
const scalar p,
|
||||
@ -367,6 +365,7 @@ Foam::scalar Foam::liquidMixture::mu
|
||||
return exp(mu);
|
||||
}
|
||||
|
||||
|
||||
Foam::scalar Foam::liquidMixture::K
|
||||
(
|
||||
const scalar p,
|
||||
@ -402,7 +401,12 @@ Foam::scalar Foam::liquidMixture::K
|
||||
{
|
||||
scalar Tj = min(TrMax*properties_[j].Tc(), T);
|
||||
|
||||
scalar Kij = 2.0/(1.0/properties_[i].K(p, Ti) + 1.0/properties_[j].K(p, Tj));
|
||||
scalar Kij =
|
||||
2.0
|
||||
/(
|
||||
1.0/properties_[i].K(p, Ti)
|
||||
+ 1.0/properties_[j].K(p, Tj)
|
||||
);
|
||||
K += phii[i]*phii[j]*Kij;
|
||||
}
|
||||
}
|
||||
@ -410,6 +414,7 @@ Foam::scalar Foam::liquidMixture::K
|
||||
return K;
|
||||
}
|
||||
|
||||
|
||||
Foam::scalar Foam::liquidMixture::D
|
||||
(
|
||||
const scalar p,
|
||||
@ -432,4 +437,5 @@ Foam::scalar Foam::liquidMixture::D
|
||||
return 1.0/Dinv;
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -27,19 +27,117 @@ License
|
||||
#include "Ar.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(Ar, 0);
|
||||
addToRunTimeSelectionTable(liquid, Ar,);
|
||||
addToRunTimeSelectionTable(liquid, Ar, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(Ar, 0);
|
||||
addToRunTimeSelectionTable(liquid, Ar,);
|
||||
addToRunTimeSelectionTable(liquid, Ar, Istream);
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
Foam::Ar::Ar()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
39.948,
|
||||
150.86,
|
||||
4.8981e+6,
|
||||
0.07459,
|
||||
0.291,
|
||||
83.78,
|
||||
6.88e+4,
|
||||
87.28,
|
||||
0.0,
|
||||
0.0,
|
||||
1.4138e+4
|
||||
),
|
||||
rho_(151.922244, 0.286, 150.86, 0.2984),
|
||||
pv_(39.233, -1051.7, -3.5895, 5.0444e-05, 2),
|
||||
hl_(150.86, 218509.061780314, 0.352, 0.0, 0.0, 0.0),
|
||||
cp_(4562.43116050866, -70.7770101131471, 0.367477721037349, 0.0, 0.0, 0.0),
|
||||
h_
|
||||
(
|
||||
-1460974.49982473,
|
||||
4562.43116050866,
|
||||
-35.3885050565735,
|
||||
0.122492573679116,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
cpg_(520.326424351657, 0.0, 0.0, 0.0, 0.0, 0.0),
|
||||
B_
|
||||
(
|
||||
0.000952488234705117,
|
||||
-0.379993992189847,
|
||||
-2022.62941824372,
|
||||
4633523580654.85,
|
||||
-302893761890458.0
|
||||
),
|
||||
mu_(-8.868, 204.3, -0.3831, -1.3e-22, 10.0),
|
||||
mug_(8.386e-07, 0.6175, 75.377, -432.5),
|
||||
K_(0.1819, -0.0003176, -4.11e-06, 0.0, 0.0, 0.0),
|
||||
Kg_(0.0001236, 0.8262, -132.8, 16000),
|
||||
sigma_(150.86, 0.03823, 1.2927, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 39.948, 28) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
|
||||
Foam::Ar::Ar
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc0& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::Ar::Ar(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
} // End namespace Foam
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
Ar()
|
||||
:
|
||||
liquid(39.948, 150.86, 4.8981e+6, 0.07459, 0.291, 83.78, 6.88e+4, 87.28, 0.0, 0.0, 1.4138e+4),
|
||||
rho_(151.922244, 0.286, 150.86, 0.2984),
|
||||
pv_(39.233, -1051.7, -3.5895, 5.0444e-05, 2),
|
||||
hl_(150.86, 218509.061780314, 0.352, 0, 0, 0),
|
||||
cp_(4562.43116050866, -70.7770101131471, 0.367477721037349, 0, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-1460974.49982473, 4562.43116050866, -35.3885050565735, 0.122492573679116, 0, 0),
|
||||
cpg_(520.326424351657, 0, 0, 0, 0, 0),
|
||||
B_(0.000952488234705117, -0.379993992189847, -2022.62941824372, 4633523580654.85, -302893761890458.0),
|
||||
mu_(-8.868, 204.3, -0.3831, -1.3e-22, 10),
|
||||
mug_(8.386e-07, 0.6175, 75.377, -432.5),
|
||||
K_(0.1819, -0.0003176, -4.11e-06, 0, 0, 0),
|
||||
Kg_(0.0001236, 0.8262, -132.8, 16000),
|
||||
sigma_(150.86, 0.03823, 1.2927, 0, 0, 0),
|
||||
D_(147.18, 20.1, 39.948, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
Ar();
|
||||
|
||||
//- Construct from components
|
||||
Ar
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
Ar(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
Ar(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const Ar& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "ArI.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/Ar/ArI.H
Normal file
105
src/thermophysicalModels/liquids/Ar/ArI.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::Ar::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::Ar::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::Ar::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::Ar::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::Ar::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::Ar::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::Ar::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::Ar::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::Ar::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::Ar::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::Ar::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::Ar::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::Ar::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C10H22.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C10H22, 0);
|
||||
addToRunTimeSelectionTable(liquid, C10H22,);
|
||||
addToRunTimeSelectionTable(liquid, C10H22, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C10H22, 0);
|
||||
addToRunTimeSelectionTable(liquid, C10H22,);
|
||||
addToRunTimeSelectionTable(liquid, C10H22, Istream);
|
||||
Foam::C10H22::C10H22()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
142.285,
|
||||
617.70,
|
||||
2.11e+6,
|
||||
0.6,
|
||||
0.247,
|
||||
243.51,
|
||||
1.393,
|
||||
447.30,
|
||||
0.0,
|
||||
0.4923,
|
||||
1.57e+4
|
||||
),
|
||||
rho_(60.94208835, 0.25745, 617.7, 0.28912),
|
||||
pv_(112.73, -9749.6, -13.245, 7.1266e-06, 2.0),
|
||||
hl_(617.70, 464743.296904101, 0.39797, 0.0, 0.0, 0.0),
|
||||
cp_
|
||||
(
|
||||
1958.18252099659,
|
||||
-1.39094071757388,
|
||||
0.00754612221948905,
|
||||
0.0,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-2699436.15229142,
|
||||
1958.18252099659,
|
||||
-0.695470358786942,
|
||||
0.00251537407316302,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
cpg_(1175.10630073444, 3762.16748076045, 1614.1, 2658.04547211582, 742),
|
||||
B_
|
||||
(
|
||||
0.00337351091119935,
|
||||
-4.13606494008504,
|
||||
-534560.916470464,
|
||||
-1.13364022911762e+19,
|
||||
2.80704220402713e+21
|
||||
),
|
||||
mu_(-16.468, 1533.5, 0.7511, 0.0, 0.0),
|
||||
mug_(2.64e-08, 0.9487, 71.0, 0.0),
|
||||
K_(0.2063, -0.000254, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(-668.4, 0.9323, -4071000000.0, 0.0),
|
||||
sigma_(617.70, 0.055435, 1.3095, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 142.285, 28.0) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C10H22::C10H22
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C10H22::C10H22(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C10H22()
|
||||
:
|
||||
liquid(142.285, 617.70, 2.11e+6, 0.6, 0.247, 243.51, 1.393, 447.30, 0.0, 0.4923, 1.57e+4),
|
||||
rho_(60.94208835, 0.25745, 617.7, 0.28912),
|
||||
pv_(112.73, -9749.6, -13.245, 7.1266e-06, 2),
|
||||
hl_(617.70, 464743.296904101, 0.39797, 0, 0, 0),
|
||||
cp_(1958.18252099659, -1.39094071757388, 0.00754612221948905, 0, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-2699436.15229142, 1958.18252099659, -0.695470358786942, 0.00251537407316302, 0, 0),
|
||||
cpg_(1175.10630073444, 3762.16748076045, 1614.1, 2658.04547211582, 742),
|
||||
B_(0.00337351091119935, -4.13606494008504, -534560.916470464, -1.13364022911762e+19, 2.80704220402713e+21),
|
||||
mu_(-16.468, 1533.5, 0.7511, 0, 0),
|
||||
mug_(2.64e-08, 0.9487, 71, 0),
|
||||
K_(0.2063, -0.000254, 0, 0, 0, 0),
|
||||
Kg_(-668.4, 0.9323, -4071000000.0, 0),
|
||||
sigma_(617.70, 0.055435, 1.3095, 0, 0, 0),
|
||||
D_(147.18, 20.1, 142.285, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C10H22();
|
||||
|
||||
//- Construct from components
|
||||
C10H22
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C10H22(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C10H22(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -261,8 +175,7 @@ public:
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C10H22& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +190,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C10H22I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C10H22/C10H22I.H
Normal file
105
src/thermophysicalModels/liquids/C10H22/C10H22I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C10H22::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C10H22::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C10H22::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C10H22::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C10H22::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C10H22::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C10H22::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C10H22::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C10H22::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C10H22::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C10H22::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C10H22::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C10H22::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,116 @@ License
|
||||
#include "C12H26.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C12H26, 0);
|
||||
addToRunTimeSelectionTable(liquid, C12H26,);
|
||||
addToRunTimeSelectionTable(liquid, C12H26, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C12H26, 0);
|
||||
addToRunTimeSelectionTable(liquid, C12H26,);
|
||||
addToRunTimeSelectionTable(liquid, C12H26, Istream);
|
||||
Foam::C12H26::C12H26()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
170.338,
|
||||
658.0,
|
||||
1.82e+6,
|
||||
0.716,
|
||||
0.238,
|
||||
263.57,
|
||||
6.152e-1,
|
||||
489.47,
|
||||
0.0,
|
||||
0.5764,
|
||||
1.59e+4
|
||||
),
|
||||
rho_(60.53982858, 0.25511, 658.0, 0.29368),
|
||||
pv_(137.47, -11976.0, -16.698, 8.0906e-06, 2.0),
|
||||
hl_(658.0, 454020.829174935, 0.40681, 0.0, 0.0, 0.0),
|
||||
cp_(2983.53861146661, -8.0352006011577, 0.018207916025784, 0.0, 0.0, 0.0),
|
||||
h_
|
||||
(
|
||||
-2755166.83820769,
|
||||
2983.53861146661,
|
||||
-4.01760030057885,
|
||||
0.00606930534192801,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
cpg_(1250.16144371778, 3894.02247296552, 1715.5, 2650.67101879792, 777.5),
|
||||
B_
|
||||
(
|
||||
0.00516619896910848,
|
||||
-6.40491258556517,
|
||||
-295295.236529723,
|
||||
-3.22147729807794e+19,
|
||||
8.78195117941974e+21
|
||||
),
|
||||
mu_(-20.607, 1943, 1.3205, 0.0, 0.0),
|
||||
mug_(6.344e-08, 0.8287, 219.5, 0.0),
|
||||
K_(0.2047, -0.0002326, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(5.719e-06, 1.4699, 579.4, 0.0),
|
||||
sigma_(658.0, 0.055493, 1.3262, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 170.338, 28.0) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C12H26::C12H26
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C12H26::C12H26(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C12H26()
|
||||
:
|
||||
liquid(170.338, 658.0, 1.82e+6, 0.716, 0.238, 263.57, 6.152e-1, 489.47, 0, 0.5764, 1.59e+4),
|
||||
rho_(60.53982858, 0.25511, 658, 0.29368),
|
||||
pv_(137.47, -11976, -16.698, 8.0906e-06, 2),
|
||||
hl_(658.0, 454020.829174935, 0.40681, 0, 0, 0),
|
||||
cp_(2983.53861146661, -8.0352006011577, 0.018207916025784, 0, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-2755166.83820769, 2983.53861146661, -4.01760030057885, 0.00606930534192801, 0, 0),
|
||||
cpg_(1250.16144371778, 3894.02247296552, 1715.5, 2650.67101879792, 777.5),
|
||||
B_(0.00516619896910848, -6.40491258556517, -295295.236529723, -3.22147729807794e+19, 8.78195117941974e+21),
|
||||
mu_(-20.607, 1943, 1.3205, 0, 0),
|
||||
mug_(6.344e-08, 0.8287, 219.5, 0),
|
||||
K_(0.2047, -0.0002326, 0, 0, 0, 0),
|
||||
Kg_(5.719e-06, 1.4699, 579.4, 0),
|
||||
sigma_(658.0, 0.055493, 1.3262, 0, 0, 0),
|
||||
D_(147.18, 20.1, 170.338, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C12H26();
|
||||
|
||||
//- Construct from conponents
|
||||
C12H26
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C12H26(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C12H26(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C12H26& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C12H26I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C12H26/C12H26I.H
Normal file
105
src/thermophysicalModels/liquids/C12H26/C12H26I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C12H26::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C12H26::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C12H26::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C12H26::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C12H26::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C12H26::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C12H26::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C12H26::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C12H26::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C12H26::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C12H26::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C12H26::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C12H26::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C13H28.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C13H28, 0);
|
||||
addToRunTimeSelectionTable(liquid, C13H28,);
|
||||
addToRunTimeSelectionTable(liquid, C13H28, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C13H28, 0);
|
||||
addToRunTimeSelectionTable(liquid, C13H28,);
|
||||
addToRunTimeSelectionTable(liquid, C13H28, Istream);
|
||||
Foam::C13H28::C13H28()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
184.365,
|
||||
675.80,
|
||||
1.7225e+6,
|
||||
0.77,
|
||||
0.236,
|
||||
267.76,
|
||||
3.801e-1,
|
||||
508.62,
|
||||
0.0,
|
||||
0.6186,
|
||||
1.5901e+4
|
||||
),
|
||||
rho_(59.513022, 0.2504, 675.8, 0.312),
|
||||
pv_(118.27, -11432, -13.769, 5.9641e-06, 2.0),
|
||||
hl_(675.80, 444227.48352453, 0.4162, 0.0, 0.0, 0.0),
|
||||
cp_
|
||||
(
|
||||
4275.05220622135,
|
||||
-16.6539202126217,
|
||||
0.0325755973205326,
|
||||
0.0,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-2860442.0545124,
|
||||
4275.05220622135,
|
||||
-8.32696010631085,
|
||||
0.0108585324401775,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
cpg_(1136.87522035093, 3641.14663846175, -1443, 2277.00485450058, -683.0),
|
||||
B_
|
||||
(
|
||||
0.00246321156401703,
|
||||
-2.66601578390692,
|
||||
-1249532.17801643,
|
||||
-1.0460770753668e+19,
|
||||
1.90117430097904e+21
|
||||
),
|
||||
mu_(-23.341, 2121.9, 1.7208, 0.0, 0.0),
|
||||
mug_(3.5585e-08, 0.8987, 165.3, 0.0),
|
||||
K_(0.1981, -0.0002046, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(5.3701e-06, 1.4751, 599.09, 0.0),
|
||||
sigma_(675.80, 0.05561, 1.3361, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 184.365, 28.0) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C13H28::C13H28
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C13H28::C13H28(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C13H28()
|
||||
:
|
||||
liquid(184.365, 675.80, 1.7225e+6, 0.77, 0.236, 267.76, 3.801e-1, 508.62, 0.0, 0.6186, 1.5901e+4),
|
||||
rho_(59.513022, 0.2504, 675.8, 0.312),
|
||||
pv_(118.27, -11432, -13.769, 5.9641e-06, 2),
|
||||
hl_(675.80, 444227.48352453, 0.4162, 0, 0, 0),
|
||||
cp_(4275.05220622135, -16.6539202126217, 0.0325755973205326, 0, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-2860442.0545124, 4275.05220622135, -8.32696010631085, 0.0108585324401775, 0, 0),
|
||||
cpg_(1136.87522035093, 3641.14663846175, -1443, 2277.00485450058, -683),
|
||||
B_(0.00246321156401703, -2.66601578390692, -1249532.17801643, -1.0460770753668e+19, 1.90117430097904e+21),
|
||||
mu_(-23.341, 2121.9, 1.7208, 0, 0),
|
||||
mug_(3.5585e-08, 0.8987, 165.3, 0),
|
||||
K_(0.1981, -0.0002046, 0, 0, 0, 0),
|
||||
Kg_(5.3701e-06, 1.4751, 599.09, 0),
|
||||
sigma_(675.80, 0.05561, 1.3361, 0, 0, 0),
|
||||
D_(147.18, 20.1, 184.365, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C13H28();
|
||||
|
||||
//- Construct from components
|
||||
C13H28
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C13H28(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C13H28(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C13H28& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C13H28I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C13H28/C13H28I.H
Normal file
105
src/thermophysicalModels/liquids/C13H28/C13H28I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C13H28::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C13H28::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C13H28::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C13H28::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C13H28::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C13H28::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C13H28::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C13H28::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C13H28::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C13H28::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C13H28::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C13H28::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C13H28::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C14H30.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C14H30, 0);
|
||||
addToRunTimeSelectionTable(liquid, C14H30,);
|
||||
addToRunTimeSelectionTable(liquid, C14H30, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C14H30, 0);
|
||||
addToRunTimeSelectionTable(liquid, C14H30,);
|
||||
addToRunTimeSelectionTable(liquid, C14H30, Istream);
|
||||
Foam::C14H30::C14H30()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
198.392,
|
||||
692.40,
|
||||
1.6212e+6,
|
||||
0.8428,
|
||||
0.237,
|
||||
279.01,
|
||||
1.8849e-1,
|
||||
526.73,
|
||||
0.0,
|
||||
0.6617,
|
||||
1.6173e+4
|
||||
),
|
||||
rho_(60.92023144, 0.2582, 692.4, 0.26628),
|
||||
pv_(249.21, -16915, -35.195, 0.028451, 1.0),
|
||||
hl_(692.40, 455764.345336506, 0.428, 0.0, 0.0, 0.0),
|
||||
cp_
|
||||
(
|
||||
2565.72845679261,
|
||||
-4.78114036856325,
|
||||
0.0120362716238558,
|
||||
0.0,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-2690601.01887934,
|
||||
2565.72845679261,
|
||||
-2.39057018428162,
|
||||
0.00401209054128527,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
cpg_(1134.11831122223, 3629.17859591113, -1440.3, 2275.29335860317, -682),
|
||||
B_
|
||||
(
|
||||
0.00247837614419936,
|
||||
-2.62692044034034,
|
||||
-1427174.48284205,
|
||||
-1.68288035807895e+19,
|
||||
3.48854792531957e+21
|
||||
),
|
||||
mu_(-18.964, 2010.9, 1.0648, 0.0, 0.0),
|
||||
mug_(4.4565e-08, 0.8684, 228.16, -4347.2),
|
||||
K_(0.1957, -0.0001993, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(-0.000628, 0.944, -5490, 0.0),
|
||||
sigma_(692.40, 0.056436, 1.3658, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 198.392, 28.0) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C14H30::C14H30
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C14H30::C14H30(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C14H30()
|
||||
:
|
||||
liquid(198.392, 692.40, 1.6212e+6, 0.8428, 0.237, 279.01, 1.8849e-1, 526.73, 0.0, 0.6617, 1.6173e+4),
|
||||
rho_(60.92023144, 0.2582, 692.4, 0.26628),
|
||||
pv_(249.21, -16915, -35.195, 0.028451, 1),
|
||||
hl_(692.40, 455764.345336506, 0.428, 0, 0, 0),
|
||||
cp_(2565.72845679261, -4.78114036856325, 0.0120362716238558, 0, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-2690601.01887934, 2565.72845679261, -2.39057018428162, 0.00401209054128527, 0, 0),
|
||||
cpg_(1134.11831122223, 3629.17859591113, -1440.3, 2275.29335860317, -682),
|
||||
B_(0.00247837614419936, -2.62692044034034, -1427174.48284205, -1.68288035807895e+19, 3.48854792531957e+21),
|
||||
mu_(-18.964, 2010.9, 1.0648, 0, 0),
|
||||
mug_(4.4565e-08, 0.8684, 228.16, -4347.2),
|
||||
K_(0.1957, -0.0001993, 0, 0, 0, 0),
|
||||
Kg_(-0.000628, 0.944, -5490, 0),
|
||||
sigma_(692.40, 0.056436, 1.3658, 0, 0, 0),
|
||||
D_(147.18, 20.1, 198.392, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C14H30();
|
||||
|
||||
//- Construct from components
|
||||
C14H30
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C14H30(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C14H30(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C14H30& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C14H30I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C14H30/C14H30I.H
Normal file
105
src/thermophysicalModels/liquids/C14H30/C14H30I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C14H30::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C14H30::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C14H30::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C14H30::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C14H30::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C14H30::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C14H30::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C14H30::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C14H30::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C14H30::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C14H30::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C14H30::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C14H30::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C16H34.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C16H34, 0);
|
||||
addToRunTimeSelectionTable(liquid, C16H34,);
|
||||
addToRunTimeSelectionTable(liquid, C16H34, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C16H34, 0);
|
||||
addToRunTimeSelectionTable(liquid, C16H34,);
|
||||
addToRunTimeSelectionTable(liquid, C16H34, Istream);
|
||||
Foam::C16H34::C16H34()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
226.446,
|
||||
720.60,
|
||||
1.4186e+6,
|
||||
0.93,
|
||||
0.22,
|
||||
291.32,
|
||||
8.7467e-2,
|
||||
560.01,
|
||||
0.0,
|
||||
0.7471,
|
||||
1.6052e+4
|
||||
),
|
||||
rho_(61.94656776, 0.25442, 720.6, 0.3238),
|
||||
pv_(233.1, -17346, -32.251, 0.02407, 1.0),
|
||||
hl_(720.60, 430654.548987397, 0.4122, 0.0, 0.0, 0.0),
|
||||
cp_
|
||||
(
|
||||
3769.90540791182,
|
||||
-12.5871068599136,
|
||||
0.0247211255663602,
|
||||
0.0,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-2777201.30410301,
|
||||
3769.90540791182,
|
||||
-6.29355342995681,
|
||||
0.00824037518878673,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
cpg_(1128.74592618108, 3600.8584828171, -1429.7, 2259.69988429913, 679.0),
|
||||
B_
|
||||
(
|
||||
0.0025091191718997,
|
||||
-2.46668079807106,
|
||||
-1704070.72767901,
|
||||
-3.00623548219001e+19,
|
||||
7.07320950690231e+21
|
||||
),
|
||||
mu_(-18.388, 2056.8, 0.98681, 0.0, 0.0),
|
||||
mug_(1.2463e-07, 0.7322, 395.0, 6000.0),
|
||||
K_(0.1963, -0.00019, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(3.075e-06, 1.552, 678.0, 0.0),
|
||||
sigma_(720.60, 0.05699, 1.3929, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 226.446, 28.0) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C16H34::C16H34
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C16H34::C16H34(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C16H34()
|
||||
:
|
||||
liquid(226.446, 720.60, 1.4186e+6, 0.93, 0.22, 291.32, 8.7467e-2, 560.01, 0, 0.7471, 1.6052e+4),
|
||||
rho_(61.94656776, 0.25442, 720.6, 0.3238),
|
||||
pv_(233.1, -17346, -32.251, 0.02407, 1),
|
||||
hl_(720.60, 430654.548987397, 0.4122, 0, 0, 0),
|
||||
cp_(3769.90540791182, -12.5871068599136, 0.0247211255663602, 0, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-2777201.30410301, 3769.90540791182, -6.29355342995681, 0.00824037518878673, 0, 0),
|
||||
cpg_(1128.74592618108, 3600.8584828171, -1429.7, 2259.69988429913, 679),
|
||||
B_(0.0025091191718997, -2.46668079807106, -1704070.72767901, -3.00623548219001e+19, 7.07320950690231e+21),
|
||||
mu_(-18.388, 2056.8, 0.98681, 0, 0),
|
||||
mug_(1.2463e-07, 0.7322, 395, 6000),
|
||||
K_(0.1963, -0.00019, 0, 0, 0, 0),
|
||||
Kg_(3.075e-06, 1.552, 678, 0),
|
||||
sigma_(720.60, 0.05699, 1.3929, 0, 0, 0),
|
||||
D_(147.18, 20.1, 226.446, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C16H34();
|
||||
|
||||
//- Construct from components
|
||||
C16H34
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C16H34(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C16H34(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C16H34& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C16H34I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C16H34/C16H34I.H
Normal file
105
src/thermophysicalModels/liquids/C16H34/C16H34I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C16H34::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C16H34::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C16H34::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C16H34::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C16H34::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C16H34::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C16H34::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C16H34::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C16H34::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C16H34::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C16H34::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C16H34::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C16H34::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C2H5OH.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C2H5OH, 0);
|
||||
addToRunTimeSelectionTable(liquid, C2H5OH,);
|
||||
addToRunTimeSelectionTable(liquid, C2H5OH, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C2H5OH, 0);
|
||||
addToRunTimeSelectionTable(liquid, C2H5OH,);
|
||||
addToRunTimeSelectionTable(liquid, C2H5OH, Istream);
|
||||
Foam::C2H5OH::C2H5OH()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
46.069,
|
||||
516.25,
|
||||
6.3835e+6,
|
||||
0.16692,
|
||||
0.248,
|
||||
159.05,
|
||||
7.1775e-5,
|
||||
351.44,
|
||||
5.6372e-30,
|
||||
0.6371,
|
||||
2.6421e+4
|
||||
),
|
||||
rho_(70.1308387, 0.26395, 516.25, 0.2367),
|
||||
pv_(59.796, -6595, -5.0474, 6.3e-07, 2),
|
||||
hl_(516.25, 958345.091059064, -0.4134, 0.75362, 0.0, 0.0),
|
||||
cp_
|
||||
(
|
||||
2052.57331394213,
|
||||
-1.21990926653498,
|
||||
0.00714146172046278,
|
||||
5.20523562482363e-05,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-6752827.25039109,
|
||||
2052.57331394213,
|
||||
-0.60995463326749,
|
||||
0.00238048724015426,
|
||||
1.30130890620591e-05,
|
||||
0.0
|
||||
),
|
||||
cpg_(909.505307256507, 3358.00646855803, 1530, 2029.56434912848, 640),
|
||||
B_
|
||||
(
|
||||
-0.00358158414552085,
|
||||
3.90718270420456,
|
||||
-1180837.43949293,
|
||||
9.81136990166923e+18,
|
||||
-3.58592545963663e+21
|
||||
),
|
||||
mu_(8.049, 776, -3.068, 0.0, 0.0),
|
||||
mug_(1.0613e-07, 0.8066, 52.7, 0.0),
|
||||
K_(0.253, -0.000281, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(-3.12, 0.7152, -3550000.0, 0.0),
|
||||
sigma_(516.25, 0.04064, -4.34e-05, -6.42e-08, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 46.069, 28) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C2H5OH::C2H5OH
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C2H5OH::C2H5OH(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C2H5OH()
|
||||
:
|
||||
liquid(46.069, 516.25, 6.3835e+6, 0.16692, 0.248, 159.05, 7.1775e-5, 351.44, 5.6372e-30, 0.6371, 2.6421e+4),
|
||||
rho_(70.1308387, 0.26395, 516.25, 0.2367),
|
||||
pv_(59.796, -6595, -5.0474, 6.3e-07, 2),
|
||||
hl_(516.25, 958345.091059064, -0.4134, 0.75362, 0, 0),
|
||||
cp_(2052.57331394213, -1.21990926653498, 0.00714146172046278, 5.20523562482363e-05, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-6752827.25039109, 2052.57331394213, -0.60995463326749, 0.00238048724015426, 1.30130890620591e-05, 0),
|
||||
cpg_(909.505307256507, 3358.00646855803, 1530, 2029.56434912848, 640),
|
||||
B_(-0.00358158414552085, 3.90718270420456, -1180837.43949293, 9.81136990166923e+18, -3.58592545963663e+21),
|
||||
mu_(8.049, 776, -3.068, 0, 0),
|
||||
mug_(1.0613e-07, 0.8066, 52.7, 0),
|
||||
K_(0.253, -0.000281, 0, 0, 0, 0),
|
||||
Kg_(-3.12, 0.7152, -3550000.0, 0),
|
||||
sigma_(516.25, 0.04064, -4.34e-05, -6.42e-08, 0, 0),
|
||||
D_(147.18, 20.1, 46.069, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C2H5OH();
|
||||
|
||||
//- Construct from components
|
||||
C2H5OH
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C2H5OH(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C2H5OH(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C2H5OH& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C2H5OHI.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C2H5OH/C2H5OHI.H
Normal file
105
src/thermophysicalModels/liquids/C2H5OH/C2H5OHI.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C2H5OH::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H5OH::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H5OH::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H5OH::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H5OH::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H5OH::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H5OH::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H5OH::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H5OH::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H5OH::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H5OH::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H5OH::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H5OH::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,115 @@ License
|
||||
#include "C2H6.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C2H6, 0);
|
||||
addToRunTimeSelectionTable(liquid, C2H6,);
|
||||
addToRunTimeSelectionTable(liquid, C2H6, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C2H6, 0);
|
||||
addToRunTimeSelectionTable(liquid, C2H6,);
|
||||
addToRunTimeSelectionTable(liquid, C2H6, Istream);
|
||||
Foam::C2H6::C2H6()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
30.070,
|
||||
305.32,
|
||||
4.872e+6,
|
||||
0.14550,
|
||||
0.279,
|
||||
90.35,
|
||||
1.13,
|
||||
184.55,
|
||||
0.0,
|
||||
0.0995,
|
||||
1.24e+4
|
||||
),
|
||||
rho_(57.499854, 0.27937, 305.32, 0.29187),
|
||||
pv_(51.857, -2598.7, -5.1283, 1.4913e-05, 2.0),
|
||||
hl_(305.32, 701396.740937812, 0.60646, -0.55492, 0.32799, 0.0),
|
||||
cp_
|
||||
(
|
||||
305.32,
|
||||
8.02554965861611,
|
||||
2983.63817758563,
|
||||
167.548325566287,
|
||||
-343.93389207094
|
||||
),
|
||||
h_(0.0, 0.0, 0.0, 0.0, 0.0, 0.0),
|
||||
cpg_(1341.07083471899, 4463.58496840705, 1655.5, 2435.08480212837, 752.87),
|
||||
B_
|
||||
(
|
||||
0.00269205187894912,
|
||||
-2.05221150648487,
|
||||
-47721.9820419022,
|
||||
2.24808779514466e+15,
|
||||
-3.23910874625873e+17
|
||||
),
|
||||
mu_(-3.4134, 197.05, -1.2193, -9.2023e-26, 10.0),
|
||||
mug_(2.5906e-07, 0.67988, 98.902, 0.0),
|
||||
K_(0.35758, -0.0011458, 6.1866e-07, 0.0, 0.0, 0.0),
|
||||
Kg_(7.3869e-05, 1.1689, 500.73, 0.0),
|
||||
sigma_(305.32, 0.048643, 1.1981, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 30.070, 28) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C2H6::C2H6
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc14& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C2H6::C2H6(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C2H6()
|
||||
:
|
||||
liquid(30.070, 305.32, 4.872e+6, 0.14550, 0.279, 90.35, 1.13, 184.55, 0.0, 0.0995, 1.24e+4),
|
||||
rho_(57.499854, 0.27937, 305.32, 0.29187),
|
||||
pv_(51.857, -2598.7, -5.1283, 1.4913e-05, 2),
|
||||
hl_(305.32, 701396.740937812, 0.60646, -0.55492, 0.32799, 0),
|
||||
cp_(305.32, 8.02554965861611, 2983.63817758563, 167.548325566287, -343.93389207094),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(0, 0, 0, 0, 0, 0),
|
||||
cpg_(1341.07083471899, 4463.58496840705, 1655.5, 2435.08480212837, 752.87),
|
||||
B_(0.00269205187894912, -2.05221150648487, -47721.9820419022, 2.24808779514466e+15, -3.23910874625873e+17),
|
||||
mu_(-3.4134, 197.05, -1.2193, -9.2023e-26, 10),
|
||||
mug_(2.5906e-07, 0.67988, 98.902, 0),
|
||||
K_(0.35758, -0.0011458, 6.1866e-07, 0, 0, 0),
|
||||
Kg_(7.3869e-05, 1.1689, 500.73, 0),
|
||||
sigma_(305.32, 0.048643, 1.1981, 0, 0, 0),
|
||||
D_(147.18, 20.1, 30.070, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C2H6();
|
||||
|
||||
//- Construct from components
|
||||
C2H6
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C2H6(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C2H6(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C2H6& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C2H6I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C2H6/C2H6I.H
Normal file
105
src/thermophysicalModels/liquids/C2H6/C2H6I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C2H6::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C2H6O.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C2H6O, 0);
|
||||
addToRunTimeSelectionTable(liquid, C2H6O,);
|
||||
addToRunTimeSelectionTable(liquid, C2H6O, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C2H6O, 0);
|
||||
addToRunTimeSelectionTable(liquid, C2H6O,);
|
||||
addToRunTimeSelectionTable(liquid, C2H6O, Istream);
|
||||
Foam::C2H6O::C2H6O()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
46.069,
|
||||
400.10,
|
||||
5.3702e+6,
|
||||
0.17,
|
||||
0.274,
|
||||
131.65,
|
||||
3.0849,
|
||||
248.31,
|
||||
4.3363e-30,
|
||||
0.2036,
|
||||
1.7572e+4
|
||||
),
|
||||
rho_(69.472052, 0.26325, 400.1, 0.2806),
|
||||
pv_(51.566, -3664.4, -4.653, 5.9e-06, 2),
|
||||
hl_(400.10, 608435.173326966, 0.2477, -0.089, 0.203, 0),
|
||||
cp_
|
||||
(
|
||||
1491.24139877141,
|
||||
11.3099915344375,
|
||||
-0.067273003538171,
|
||||
0.000136556035511949,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-5024829.22619402,
|
||||
1491.24139877141,
|
||||
5.65499576721874,
|
||||
-0.0224243345127237,
|
||||
3.41390088779874e-05,
|
||||
0.0
|
||||
),
|
||||
cpg_(950.747791356443, 3160.47667628991, 1284, 1291.5409494454, 520),
|
||||
B_
|
||||
(
|
||||
0.00235082159369641,
|
||||
-2.26616596843865,
|
||||
-123293.320888233,
|
||||
-8.87364605266014e+16,
|
||||
1.46389111984198e+19
|
||||
),
|
||||
mu_(-10.62, 448.99, 8.3967e-05, 0.0, 0.0),
|
||||
mug_(7.27, 0.1091, 440600000, 0.0),
|
||||
K_(0.31276, -0.0005677, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(0.2247, 0.1026, 997.06, 1762900),
|
||||
sigma_(400.10, 0.06096, 1.2286, 0, 0, 0),
|
||||
D_(147.18, 20.1, 46.069, 28) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C2H6O::C2H6O
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C2H6O::C2H6O(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C2H6O()
|
||||
:
|
||||
liquid(46.069, 400.10, 5.3702e+6, 0.17, 0.274, 131.65, 3.0849, 248.31, 4.3363e-30, 0.2036, 1.7572e+4),
|
||||
rho_(69.472052, 0.26325, 400.1, 0.2806),
|
||||
pv_(51.566, -3664.4, -4.653, 5.9e-06, 2),
|
||||
hl_(400.10, 608435.173326966, 0.2477, -0.089, 0.203, 0),
|
||||
cp_(1491.24139877141, 11.3099915344375, -0.067273003538171, 0.000136556035511949, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-5024829.22619402, 1491.24139877141, 5.65499576721874, -0.0224243345127237, 3.41390088779874e-05, 0),
|
||||
cpg_(950.747791356443, 3160.47667628991, 1284, 1291.5409494454, 520),
|
||||
B_(0.00235082159369641, -2.26616596843865, -123293.320888233, -8.87364605266014e+16, 1.46389111984198e+19),
|
||||
mu_(-10.62, 448.99, 8.3967e-05, 0, 0),
|
||||
mug_(7.27, 0.1091, 440600000, 0),
|
||||
K_(0.31276, -0.0005677, 0, 0, 0, 0),
|
||||
Kg_(0.2247, 0.1026, 997.06, 1762900),
|
||||
sigma_(400.10, 0.06096, 1.2286, 0, 0, 0),
|
||||
D_(147.18, 20.1, 46.069, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C2H6O();
|
||||
|
||||
//- Construct from components
|
||||
C2H6O
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C2H6O(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C2H6O(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C2H6O& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C2H6OI.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C2H6O/C2H6OI.H
Normal file
105
src/thermophysicalModels/liquids/C2H6O/C2H6OI.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C2H6O::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6O::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6O::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6O::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6O::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6O::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6O::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6O::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6O::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6O::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6O::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6O::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C2H6O::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C3H6O.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C3H6O, 0);
|
||||
addToRunTimeSelectionTable(liquid, C3H6O,);
|
||||
addToRunTimeSelectionTable(liquid, C3H6O, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C3H6O, 0);
|
||||
addToRunTimeSelectionTable(liquid, C3H6O,);
|
||||
addToRunTimeSelectionTable(liquid, C3H6O, Istream);
|
||||
Foam::C3H6O::C3H6O()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
58.08,
|
||||
508.20,
|
||||
4.7015e+6,
|
||||
0.209,
|
||||
0.233,
|
||||
178.45,
|
||||
2.5938,
|
||||
329.44,
|
||||
9.6066e-30,
|
||||
0.3064,
|
||||
1.9774e+4
|
||||
),
|
||||
rho_(71.426784, 0.2576, 508.2, 0.29903),
|
||||
pv_(70.72, -5.685, -7.351, 6.3e-06, 2.0),
|
||||
hl_(508.20, 846590.909090909, 1.036, -1.294, 0.672, 0.0),
|
||||
cp_
|
||||
(
|
||||
2334.71074380165,
|
||||
-3.04752066115702,
|
||||
0.00488464187327824,
|
||||
1.18629476584022e-05,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
2571201.780143,
|
||||
2334.71074380165,
|
||||
-1.52376033057851,
|
||||
0.00162821395775941,
|
||||
2.96573691460055e-06,
|
||||
0.0
|
||||
),
|
||||
cpg_(828.512396694215, 2830.57851239669, 1250.0, 1234.50413223141, -524.4),
|
||||
B_
|
||||
(
|
||||
0.00190599173553719,
|
||||
-1.70798898071625,
|
||||
-525826.446280992,
|
||||
1.70282369146006e+17,
|
||||
-2.83298898071625e+20
|
||||
),
|
||||
mu_(-14.918, 1023.4, 0.5961, 0.0, 0.0),
|
||||
mug_(3.1005e-08, 0.9762, 23.139, 0.0),
|
||||
K_(0.2502, -0.000298, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(-26.8, 0.9098, -126500000, 0.0),
|
||||
sigma_(508.20, 0.0622, 1.124, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 58.08, 28) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C3H6O::C3H6O
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C3H6O::C3H6O(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C3H6O()
|
||||
:
|
||||
liquid(58.08, 508.20, 4.7015e+6, 0.209, 0.233, 178.45, 2.5938, 329.44, 9.6066e-30, 0.3064, 1.9774e+4),
|
||||
rho_(71.426784, 0.2576, 508.2, 0.29903),
|
||||
pv_(70.72, -5.685, -7.351, 6.3e-06, 2),
|
||||
hl_(508.20, 846590.909090909, 1.036, -1.294, 0.672, 0),
|
||||
cp_(2334.71074380165, -3.04752066115702, 0.00488464187327824, 1.18629476584022e-05, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(2571201.780143, 2334.71074380165, -1.52376033057851, 0.00162821395775941, 2.96573691460055e-06, 0),
|
||||
cpg_(828.512396694215, 2830.57851239669, 1250, 1234.50413223141, -524.4),
|
||||
B_(0.00190599173553719, -1.70798898071625, -525826.446280992, 1.70282369146006e+17, -2.83298898071625e+20),
|
||||
mu_(-14.918, 1023.4, 0.5961, 0, 0),
|
||||
mug_(3.1005e-08, 0.9762, 23.139, 0),
|
||||
K_(0.2502, -0.000298, 0, 0, 0, 0),
|
||||
Kg_(-26.8, 0.9098, -126500000, 0),
|
||||
sigma_(508.20, 0.0622, 1.124, 0, 0, 0),
|
||||
D_(147.18, 20.1, 58.08, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C3H6O();
|
||||
|
||||
//- Construct from compoents
|
||||
C3H6O
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C3H6O(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C3H6O(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,8 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
//- Ostream Operator
|
||||
|
||||
friend Ostream& operator<<(Ostream& os, const C3H6O& l)
|
||||
{
|
||||
@ -277,6 +190,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C3H6OI.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
104
src/thermophysicalModels/liquids/C3H6O/C3H6OI.H
Normal file
104
src/thermophysicalModels/liquids/C3H6O/C3H6OI.H
Normal file
@ -0,0 +1,104 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C3H6O::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H6O::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H6O::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H6O::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H6O::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H6O::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H6O::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H6O::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H6O::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H6O::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H6O::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H6O::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H6O::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,113 @@ License
|
||||
#include "C3H8.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C3H8, 0);
|
||||
addToRunTimeSelectionTable(liquid, C3H8,);
|
||||
addToRunTimeSelectionTable(liquid, C3H8, Istream);
|
||||
}
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
Foam::C3H8::C3H8()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
44.096,
|
||||
369.83,
|
||||
4.248e+6,
|
||||
0.2, 0.276,
|
||||
85.47,
|
||||
1.685e-4,
|
||||
231.11,
|
||||
0.0,
|
||||
0.1523,
|
||||
1.31e+4
|
||||
),
|
||||
rho_(60.6628672, 0.27453, 369.83, 0.29359),
|
||||
pv_(59.078, -3492.6, -6.0669, 1.0919e-05, 2.0),
|
||||
hl_(369.83, 662395.682148041, 0.78237, -0.77319, 0.39246, 0.0),
|
||||
cp_
|
||||
(
|
||||
369.83,
|
||||
9.48470319647089,
|
||||
2576.87772133527,
|
||||
95.3560311677331,
|
||||
-131.535634282099
|
||||
),
|
||||
h_(0.0, 0.0, 0.0, 0.0, 0.0, 0.0),
|
||||
cpg_(1177.43105950653, 4364.34143686502, 1626.5, 2648.76632801161, 723.6),
|
||||
B_
|
||||
(
|
||||
0.00255578737300435,
|
||||
-2.24963715529753,
|
||||
-102276.850507983,
|
||||
7.00743831640058e+15,
|
||||
-1.59878447024673e+18
|
||||
),
|
||||
mu_(-6.9281, 420.76, -0.63276, -1.713e-26, 10.0),
|
||||
mug_(2.4993e-07, 0.68612, 179.34, -8254.6),
|
||||
K_(0.26755, -0.00066457, 2.774e-07, 0.0, 0.0, 0.0),
|
||||
Kg_(-1.12, 0.10972, -9834.6, -7535800),
|
||||
sigma_(369.83, 0.05092, 1.2197, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 44.096, 28) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
defineTypeNameAndDebug(C3H8, 0);
|
||||
addToRunTimeSelectionTable(liquid, C3H8,);
|
||||
addToRunTimeSelectionTable(liquid, C3H8, Istream);
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
Foam::C3H8::C3H8
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc14& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C3H8::C3H8(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
} // End namespace Foam
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C3H8()
|
||||
:
|
||||
liquid(44.096, 369.83, 4.248e+6, 0.2, 0.276, 85.47, 1.685e-4, 231.11, 0.0, 0.1523, 1.31e+4),
|
||||
rho_(60.6628672, 0.27453, 369.83, 0.29359),
|
||||
pv_(59.078, -3492.6, -6.0669, 1.0919e-05, 2),
|
||||
hl_(369.83, 662395.682148041, 0.78237, -0.77319, 0.39246, 0),
|
||||
cp_(369.83, 9.48470319647089, 2576.87772133527, 95.3560311677331, -131.535634282099),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(0, 0, 0, 0, 0, 0),
|
||||
cpg_(1177.43105950653, 4364.34143686502, 1626.5, 2648.76632801161, 723.6),
|
||||
B_(0.00255578737300435, -2.24963715529753, -102276.850507983, 7.00743831640058e+15, -1.59878447024673e+18),
|
||||
mu_(-6.9281, 420.76, -0.63276, -1.713e-26, 10),
|
||||
mug_(2.4993e-07, 0.68612, 179.34, -8254.6),
|
||||
K_(0.26755, -0.00066457, 2.774e-07, 0, 0, 0),
|
||||
Kg_(-1.12, 0.10972, -9834.6, -7535800),
|
||||
sigma_(369.83, 0.05092, 1.2197, 0, 0, 0),
|
||||
D_(147.18, 20.1, 44.096, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C3H8();
|
||||
|
||||
//- Construct from components
|
||||
C3H8
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C3H8(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C3H8(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C3H8& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C3H8I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C3H8/C3H8I.H
Normal file
105
src/thermophysicalModels/liquids/C3H8/C3H8I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C3H8::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H8::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H8::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H8::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H8::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H8::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H8::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H8::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H8::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H8::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H8::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H8::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C3H8::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C4H10O.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C4H10O, 0);
|
||||
addToRunTimeSelectionTable(liquid, C4H10O,);
|
||||
addToRunTimeSelectionTable(liquid, C4H10O, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C4H10O, 0);
|
||||
addToRunTimeSelectionTable(liquid, C4H10O,);
|
||||
addToRunTimeSelectionTable(liquid, C4H10O, Istream);
|
||||
Foam::C4H10O::C4H10O()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
74.123,
|
||||
466.70,
|
||||
3.6376e+6,
|
||||
0.28,
|
||||
0.262,
|
||||
156.85,
|
||||
4.0709e-1,
|
||||
307.58,
|
||||
3.836e-30,
|
||||
0.2846,
|
||||
1.5532e+4
|
||||
),
|
||||
rho_(75.2793188, 0.27608, 466.7, 0.29358),
|
||||
pv_(101.03, -6311.5, -12.27, 1.377e-05, 2),
|
||||
hl_(466.70, 566355.921913576, 0.40717, 0, 0, 0),
|
||||
cp_
|
||||
(
|
||||
599.004357621791,
|
||||
17.5519069654493,
|
||||
-0.0742009902459426,
|
||||
0.00011822241409549,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-4312350.92187216,
|
||||
599.004357621791,
|
||||
8.77595348272466,
|
||||
-0.0247336634153142,
|
||||
2.95556035238725e-05,
|
||||
0.0
|
||||
),
|
||||
cpg_(1163.06679438231, 3441.57683849817, 1541.3, 1938.66950878944, -688.9),
|
||||
B_
|
||||
(
|
||||
0.00215992337061371,
|
||||
-1.810504162001,
|
||||
-276972.0599544,
|
||||
-2.12349742994752e+17,
|
||||
3.1016013922804e+19
|
||||
),
|
||||
mu_(10.197, -63.8, -3.226, 0.0, 0.0),
|
||||
mug_(1.948e-06, 0.41, 495.8, 0.0),
|
||||
K_(0.249, -0.0004005, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(-0.0044894, 0.6155, -3266.3, 0.0),
|
||||
sigma_(466.70, 0.057356, 1.288, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 74.123, 28) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C4H10O::C4H10O
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C4H10O::C4H10O(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C4H10O()
|
||||
:
|
||||
liquid(74.123, 466.70, 3.6376e+6, 0.28, 0.262, 156.85, 4.0709e-1, 307.58, 3.836e-30, 0.2846, 1.5532e+4),
|
||||
rho_(75.2793188, 0.27608, 466.7, 0.29358),
|
||||
pv_(101.03, -6311.5, -12.27, 1.377e-05, 2),
|
||||
hl_(466.70, 566355.921913576, 0.40717, 0, 0, 0),
|
||||
cp_(599.004357621791, 17.5519069654493, -0.0742009902459426, 0.00011822241409549, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-4312350.92187216, 599.004357621791, 8.77595348272466, -0.0247336634153142, 2.95556035238725e-05, 0),
|
||||
cpg_(1163.06679438231, 3441.57683849817, 1541.3, 1938.66950878944, -688.9),
|
||||
B_(0.00215992337061371, -1.810504162001, -276972.0599544, -2.12349742994752e+17, 3.1016013922804e+19),
|
||||
mu_(10.197, -63.8, -3.226, 0, 0),
|
||||
mug_(1.948e-06, 0.41, 495.8, 0),
|
||||
K_(0.249, -0.0004005, 0, 0, 0, 0),
|
||||
Kg_(-0.0044894, 0.6155, -3266.3, 0),
|
||||
sigma_(466.70, 0.057356, 1.288, 0, 0, 0),
|
||||
D_(147.18, 20.1, 74.123, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C4H10O();
|
||||
|
||||
//- Construct from components
|
||||
C4H10O
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C4H10O(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C4H10O(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C4H10O& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C4H10OI.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C4H10O/C4H10OI.H
Normal file
105
src/thermophysicalModels/liquids/C4H10O/C4H10OI.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C4H10O::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C4H10O::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C4H10O::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C4H10O::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C4H10O::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C4H10O::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C4H10O::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C4H10O::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C4H10O::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C4H10O::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C4H10O::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C4H10O::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C4H10O::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C6H14.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C6H14, 0);
|
||||
addToRunTimeSelectionTable(liquid, C6H14,);
|
||||
addToRunTimeSelectionTable(liquid, C6H14, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C6H14, 0);
|
||||
addToRunTimeSelectionTable(liquid, C6H14,);
|
||||
addToRunTimeSelectionTable(liquid, C6H14, Istream);
|
||||
Foam::C6H14::C6H14()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
86.177,
|
||||
507.60,
|
||||
3.025e+6,
|
||||
0.371,
|
||||
0.266,
|
||||
177.83,
|
||||
9.017e-1,
|
||||
341.88,
|
||||
0.0,
|
||||
0.3013,
|
||||
1.49e+4
|
||||
),
|
||||
rho_(61.03399848, 0.26411, 507.6, 0.27537),
|
||||
pv_(104.65, -6995.5, -12.702, 1.2381e-05, 2.0),
|
||||
hl_(507.60, 527286.863084118, 0.39002, 0.0, 0.0, 0.0),
|
||||
cp_
|
||||
(
|
||||
1997.28465831951,
|
||||
-2.13258758137322,
|
||||
0.0102964828202421,
|
||||
0.0,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-2902186.5403246,
|
||||
1997.28465831951,
|
||||
-1.06629379068661,
|
||||
0.00343216094008069,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
cpg_(1211.4601343746, 4088.0977523005, 1694.6, 2748.99335089409, 761.6),
|
||||
B_
|
||||
(
|
||||
0.0022859927822969,
|
||||
-2.32080485512376,
|
||||
-430509.300625457,
|
||||
1.93787205402834e+17,
|
||||
-7.17128700233241e+19
|
||||
),
|
||||
mu_(-20.715, 1207.5, 1.4993, 0.0, 0.0),
|
||||
mug_(1.7514e-07, 0.70737, 157.14, 0.0),
|
||||
K_(0.22492, -0.0003533, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(-650.5, 0.8053, -1412100000, 0.0),
|
||||
sigma_(507.60, 0.055003, 1.2674, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 86.177, 28) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C6H14::C6H14
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C6H14::C6H14(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C6H14()
|
||||
:
|
||||
liquid(86.177, 507.60, 3.025e+6, 0.371, 0.266, 177.83, 9.017e-1, 341.88, 0.0, 0.3013, 1.49e+4),
|
||||
rho_(61.03399848, 0.26411, 507.6, 0.27537),
|
||||
pv_(104.65, -6995.5, -12.702, 1.2381e-05, 2),
|
||||
hl_(507.60, 527286.863084118, 0.39002, 0, 0, 0),
|
||||
cp_(1997.28465831951, -2.13258758137322, 0.0102964828202421, 0, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-2902186.5403246, 1997.28465831951, -1.06629379068661, 0.00343216094008069, 0, 0),
|
||||
cpg_(1211.4601343746, 4088.0977523005, 1694.6, 2748.99335089409, 761.6),
|
||||
B_(0.0022859927822969, -2.32080485512376, -430509.300625457, 1.93787205402834e+17, -7.17128700233241e+19),
|
||||
mu_(-20.715, 1207.5, 1.4993, 0, 0),
|
||||
mug_(1.7514e-07, 0.70737, 157.14, 0),
|
||||
K_(0.22492, -0.0003533, 0, 0, 0, 0),
|
||||
Kg_(-650.5, 0.8053, -1412100000, 0),
|
||||
sigma_(507.60, 0.055003, 1.2674, 0, 0, 0),
|
||||
D_(147.18, 20.1, 86.177, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C6H14();
|
||||
|
||||
//- Construct from components
|
||||
C6H14
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C6H14(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C6H14(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C6H14& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C6H14I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C6H14/C6H14I.H
Normal file
105
src/thermophysicalModels/liquids/C6H14/C6H14I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C6H14::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H14::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H14::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H14::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H14::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H14::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H14::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H14::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H14::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H14::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H14::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H14::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H14::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C6H6.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C6H6, 0);
|
||||
addToRunTimeSelectionTable(liquid, C6H6,);
|
||||
addToRunTimeSelectionTable(liquid, C6H6, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C6H6, 0);
|
||||
addToRunTimeSelectionTable(liquid, C6H6,);
|
||||
addToRunTimeSelectionTable(liquid, C6H6, Istream);
|
||||
Foam::C6H6::C6H6()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
78.114,
|
||||
562.16,
|
||||
4.898e+6,
|
||||
0.25894,
|
||||
0.271,
|
||||
278.68,
|
||||
4.7961e+3,
|
||||
353.24,
|
||||
0.0,
|
||||
0.2108,
|
||||
1.8706e+4
|
||||
),
|
||||
rho_(80.5511568, 0.2667, 562.16, 0.2818),
|
||||
pv_(78.05, -6275.5, -8.4443, 6.26e-06, 2),
|
||||
hl_(562.16, 649435.440510024, 0.7616, -0.5052, 0.1564, 0),
|
||||
cp_
|
||||
(
|
||||
1386.69124612745,
|
||||
-0.416058581048212,
|
||||
0.00542796425736744,
|
||||
0.0,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
186141.395065592,
|
||||
1386.69124612745,
|
||||
-0.208029290524106,
|
||||
0.00180932141912248,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
cpg_(568.656066774202, 2970.65826868423, 1494.6, 2203.57426325627, -678.15),
|
||||
B_
|
||||
(
|
||||
0.00184089919860716,
|
||||
-2.30176408838364,
|
||||
-309176.332027549,
|
||||
-5.12072099751645e+15,
|
||||
-2.90216862534245e+19
|
||||
),
|
||||
mu_(6.764, 336.4, -2.687, 0.0, 0.0),
|
||||
mug_(3.134e-08, 0.9676, 7.9, 0.0),
|
||||
K_(0.2407, -0.0003202, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(1.652e-05, 1.3117, 491, 0.0),
|
||||
sigma_(562.16, 0.07195, 1.2389, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 78.114, 28) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C6H6::C6H6
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C6H6::C6H6(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C6H6()
|
||||
:
|
||||
liquid(78.114, 562.16, 4.898e+6, 0.25894, 0.271, 278.68, 4.7961e+3, 353.24, 0.0, 0.2108, 1.8706e+4),
|
||||
rho_(80.5511568, 0.2667, 562.16, 0.2818),
|
||||
pv_(78.05, -6275.5, -8.4443, 6.26e-06, 2),
|
||||
hl_(562.16, 649435.440510024, 0.7616, -0.5052, 0.1564, 0),
|
||||
cp_(1386.69124612745, -0.416058581048212, 0.00542796425736744, 0, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(186141.395065592, 1386.69124612745, -0.208029290524106, 0.00180932141912248, 0, 0),
|
||||
cpg_(568.656066774202, 2970.65826868423, 1494.6, 2203.57426325627, -678.15),
|
||||
B_(0.00184089919860716, -2.30176408838364, -309176.332027549, -5.12072099751645e+15, -2.90216862534245e+19),
|
||||
mu_(6.764, 336.4, -2.687, 0, 0),
|
||||
mug_(3.134e-08, 0.9676, 7.9, 0),
|
||||
K_(0.2407, -0.0003202, 0, 0, 0, 0),
|
||||
Kg_(1.652e-05, 1.3117, 491, 0),
|
||||
sigma_(562.16, 0.07195, 1.2389, 0, 0, 0),
|
||||
D_(147.18, 20.1, 78.114, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C6H6();
|
||||
|
||||
//- Comstruct from components
|
||||
C6H6
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C6H6(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C6H6(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C6H6& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C6H6I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C6H6/C6H6I.H
Normal file
105
src/thermophysicalModels/liquids/C6H6/C6H6I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C6H6::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H6::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H6::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H6::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H6::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H6::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H6::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H6::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H6::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H6::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H6::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H6::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C6H6::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,115 @@ License
|
||||
#include "C7H16.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C7H16, 0);
|
||||
addToRunTimeSelectionTable(liquid, C7H16,);
|
||||
addToRunTimeSelectionTable(liquid, C7H16, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C7H16, 0);
|
||||
addToRunTimeSelectionTable(liquid, C7H16,);
|
||||
addToRunTimeSelectionTable(liquid, C7H16, Istream);
|
||||
Foam::C7H16::C7H16()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
100.204,
|
||||
540.20,
|
||||
2.74e+6,
|
||||
0.428,
|
||||
0.261,
|
||||
182.57,
|
||||
1.8269e-1,
|
||||
371.58,
|
||||
0.0,
|
||||
0.3495,
|
||||
1.52e+4
|
||||
),
|
||||
rho_(61.38396836, 0.26211, 540.2, 0.28141),
|
||||
pv_(87.829, -6996.4, -9.8802, 7.2099e-06, 2.0),
|
||||
hl_(540.20, 499121.791545248, 0.38795, 0.0, 0.0, 0.0),
|
||||
cp_
|
||||
(
|
||||
540.20,
|
||||
6.11976102401216,
|
||||
3137.69909384855,
|
||||
182.274175063868,
|
||||
-254.530511150515
|
||||
),
|
||||
h_(-3.1469964e+6,7.3072e+3,-3.52884e+1,1.10637e-1,-1.634831e-4,9.64941e-8),
|
||||
cpg_(1199.05392998284, 3992.85457666361, 1676.6, 2734.42177956968, 756.4),
|
||||
B_
|
||||
(
|
||||
0.00274040956448844,
|
||||
-2.90407568560137,
|
||||
-440900.562851782,
|
||||
-8.78208454752305e+17,
|
||||
1.28238393676899e+20
|
||||
),
|
||||
mu_(-24.451, 1533.1, 2.0087, 0.0, 0.0),
|
||||
mug_(6.672e-08, 0.82837, 85.752, 0.0),
|
||||
K_(0.215, -0.000303, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(-0.070028, 0.38068, -7049.9, -2400500.0),
|
||||
sigma_(540.20, 0.054143, 1.2512, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 100.204, 28.0) // note: Same as C7H16
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C7H16::C7H16
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc14& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C7H16::C7H16(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C7H16()
|
||||
:
|
||||
liquid(100.204, 540.20, 2.74e+6, 0.428, 0.261, 182.57, 1.8269e-1, 371.58, 0, 0.3495, 1.52e+4),
|
||||
rho_(61.38396836, 0.26211, 540.2, 0.28141),
|
||||
pv_(87.829, -6996.4, -9.8802, 7.2099e-06, 2),
|
||||
hl_(540.20, 499121.791545248, 0.38795, 0, 0, 0),
|
||||
cp_(540.20, 6.11976102401216, 3137.69909384855, 182.274175063868, -254.530511150515),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-3.1469964e+6,7.3072e+3,-3.52884e+1,1.10637e-1,-1.634831e-4,9.64941e-8),
|
||||
cpg_(1199.05392998284, 3992.85457666361, 1676.6, 2734.42177956968, 756.4),
|
||||
B_(0.00274040956448844, -2.90407568560137, -440900.562851782, -8.78208454752305e+17, 1.28238393676899e+20),
|
||||
mu_(-24.451, 1533.1, 2.0087, 0, 0),
|
||||
mug_(6.672e-08, 0.82837, 85.752, 0),
|
||||
K_(0.215, -0.000303, 0, 0, 0, 0),
|
||||
Kg_(-0.070028, 0.38068, -7049.9, -2400500),
|
||||
sigma_(540.20, 0.054143, 1.2512, 0, 0, 0),
|
||||
D_(147.18, 20.1, 100.204, 28) // NN: Same as C7H16
|
||||
{}
|
||||
C7H16();
|
||||
|
||||
//- Construct from components
|
||||
C7H16
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C7H16(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C7H16(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C7H16& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C7H16I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C7H16/C7H16I.H
Normal file
105
src/thermophysicalModels/liquids/C7H16/C7H16I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C7H16::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H16::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H16::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H16::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H16::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H16::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H16::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H16::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H16::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H16::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H16::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H16::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H16::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C7H8.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C7H8, 0);
|
||||
addToRunTimeSelectionTable(liquid, C7H8,);
|
||||
addToRunTimeSelectionTable(liquid, C7H8, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C7H8, 0);
|
||||
addToRunTimeSelectionTable(liquid, C7H8,);
|
||||
addToRunTimeSelectionTable(liquid, C7H8, Istream);
|
||||
Foam::C7H8::C7H8()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
92.141,
|
||||
591.79,
|
||||
4.1086e+6,
|
||||
0.31579,
|
||||
0.264,
|
||||
178.18,
|
||||
4.1009e-2,
|
||||
383.78,
|
||||
1.2008e-30,
|
||||
0.2641,
|
||||
1.8346e+4
|
||||
),
|
||||
rho_(81.32088237, 0.27108, 591.79, 0.29889),
|
||||
pv_(83.359, -6995, -9.1635, 6.225e-06, 2.0),
|
||||
hl_(591.79, 544383.065085033, 0.3834, 0.0, 0.0, 0.0),
|
||||
cp_
|
||||
(
|
||||
2066.83235476064,
|
||||
-8.14664481609707,
|
||||
0.0322581695445024,
|
||||
-3.01223125427334e-05,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-353094.830249075,
|
||||
2066.83235476064,
|
||||
-4.07332240804853,
|
||||
0.0107527231815008,
|
||||
-7.53057813568336e-06,
|
||||
0.0
|
||||
),
|
||||
cpg_(630.989461803106, 3107.19440856947, 1440.6, 2059.88647833212, -650.43),
|
||||
B_
|
||||
(
|
||||
0.00191120131103418,
|
||||
-2.24970425760519,
|
||||
-482293.441573241,
|
||||
-7.62309938029759e+17,
|
||||
1.00986531511488e+20
|
||||
),
|
||||
mu_(-13.362, 1183, 0.333, 0.0, 0.0),
|
||||
mug_(2.919e-08, 0.9648, 0.0, 0.0),
|
||||
K_(0.2043, -0.000239, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(2.392e-05, 1.2694, 537, 0.0),
|
||||
sigma_(591.79, 0.06685, 1.2456, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 92.141, 28) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C7H8::C7H8
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C7H8::C7H8(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C7H8()
|
||||
:
|
||||
liquid(92.141, 591.79, 4.1086e+6, 0.31579, 0.264, 178.18, 4.1009e-2, 383.78, 1.2008e-30, 0.2641, 1.8346e+4),
|
||||
rho_(81.32088237, 0.27108, 591.79, 0.29889),
|
||||
pv_(83.359, -6995, -9.1635, 6.225e-06, 2),
|
||||
hl_(591.79, 544383.065085033, 0.3834, 0, 0, 0),
|
||||
cp_(2066.83235476064, -8.14664481609707, 0.0322581695445024, -3.01223125427334e-05, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-353094.830249075, 2066.83235476064, -4.07332240804853, 0.0107527231815008, -7.53057813568336e-06, 0),
|
||||
cpg_(630.989461803106, 3107.19440856947, 1440.6, 2059.88647833212, -650.43),
|
||||
B_(0.00191120131103418, -2.24970425760519, -482293.441573241, -7.62309938029759e+17, 1.00986531511488e+20),
|
||||
mu_(-13.362, 1183, 0.333, 0, 0),
|
||||
mug_(2.919e-08, 0.9648, 0, 0),
|
||||
K_(0.2043, -0.000239, 0, 0, 0, 0),
|
||||
Kg_(2.392e-05, 1.2694, 537, 0),
|
||||
sigma_(591.79, 0.06685, 1.2456, 0, 0, 0),
|
||||
D_(147.18, 20.1, 92.141, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C7H8();
|
||||
|
||||
//- Construct from components
|
||||
C7H8
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C7H8(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C7H8(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C7H8& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C7H8I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C7H8/C7H8I.H
Normal file
105
src/thermophysicalModels/liquids/C7H8/C7H8I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C7H8::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H8::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H8::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H8::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H8::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H8::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H8::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H8::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H8::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H8::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H8::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H8::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C7H8::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C8H10.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C8H10, 0);
|
||||
addToRunTimeSelectionTable(liquid, C8H10,);
|
||||
addToRunTimeSelectionTable(liquid, C8H10, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C8H10, 0);
|
||||
addToRunTimeSelectionTable(liquid, C8H10,);
|
||||
addToRunTimeSelectionTable(liquid, C8H10, Istream);
|
||||
Foam::C8H10::C8H10()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
106.167,
|
||||
617.17,
|
||||
3.6094e+6,
|
||||
0.37381,
|
||||
0.263,
|
||||
178.15,
|
||||
4.038e-3,
|
||||
409.35,
|
||||
1.9680e-30,
|
||||
0.3036,
|
||||
1.8043e+4
|
||||
),
|
||||
rho_(76.3765398, 0.26438, 617.17, 0.2921),
|
||||
pv_(88.246, -7691.1, -9.797, 5.931e-06, 2.0),
|
||||
hl_(617.17, 516167.924119547, 0.3882, 0.0, 0.0, 0.0),
|
||||
cp_
|
||||
(
|
||||
818.521762883005,
|
||||
6.66873887366131,
|
||||
-0.0248005500767658,
|
||||
4.23860521631015e-05,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-524002.612929508,
|
||||
818.521762883005,
|
||||
3.33436943683065,
|
||||
-0.00826685002558862,
|
||||
1.05965130407754e-05,
|
||||
0.0
|
||||
),
|
||||
cpg_(738.835984816374, 3201.5598067196, 1559, 2285.07916772632, -702.0),
|
||||
B_
|
||||
(
|
||||
0.00165776559571242,
|
||||
-2.77958310962917,
|
||||
-388067.855359952,
|
||||
-5.86905535618412e+18,
|
||||
1.58052878954854e+21
|
||||
),
|
||||
mu_(-10.452, 1048.4, -0.0715, 0.0, 0.0),
|
||||
mug_(1.2e-06, 0.4518, 439.0, 0.0),
|
||||
K_(0.20149, -0.00023988, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(1.708e-05, 1.319, 565.6, 0.0),
|
||||
sigma_(617.17, 0.066, 1.268, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 106.167, 28.0) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C8H10::C8H10
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C8H10::C8H10(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -86,26 +86,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C8H10()
|
||||
:
|
||||
liquid(106.167, 617.17, 3.6094e+6, 0.37381, 0.263, 178.15, 4.038e-3, 409.35, 1.9680e-30, 0.3036, 1.8043e+4),
|
||||
rho_(76.3765398, 0.26438, 617.17, 0.2921),
|
||||
pv_(88.246, -7691.1, -9.797, 5.931e-06, 2),
|
||||
hl_(617.17, 516167.924119547, 0.3882, 0, 0, 0),
|
||||
cp_(818.521762883005, 6.66873887366131, -0.0248005500767658, 4.23860521631015e-05, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-524002.612929508, 818.521762883005, 3.33436943683065, -0.00826685002558862, 1.05965130407754e-05, 0),
|
||||
cpg_(738.835984816374, 3201.5598067196, 1559, 2285.07916772632, -702),
|
||||
B_(0.00165776559571242, -2.77958310962917, -388067.855359952, -5.86905535618412e+18, 1.58052878954854e+21),
|
||||
mu_(-10.452, 1048.4, -0.0715, 0, 0),
|
||||
mug_(1.2e-06, 0.4518, 439, 0),
|
||||
K_(0.20149, -0.00023988, 0, 0, 0, 0),
|
||||
Kg_(1.708e-05, 1.319, 565.6, 0),
|
||||
sigma_(617.17, 0.066, 1.268, 0, 0, 0),
|
||||
D_(147.18, 20.1, 106.167, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C8H10();
|
||||
|
||||
// Construct from components
|
||||
C8H10
|
||||
(
|
||||
const liquid& l,
|
||||
@ -122,125 +105,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C8H10(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C8H10(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -259,9 +173,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C8H10& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -276,6 +188,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C8H10I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C8H10/C8H10I.H
Normal file
105
src/thermophysicalModels/liquids/C8H10/C8H10I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C8H10::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H10::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H10::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H10::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H10::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H10::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H10::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H10::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H10::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H10::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H10::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H10::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H10::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C8H18.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C8H18, 0);
|
||||
addToRunTimeSelectionTable(liquid, C8H18,);
|
||||
addToRunTimeSelectionTable(liquid, C8H18, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C8H18, 0);
|
||||
addToRunTimeSelectionTable(liquid, C8H18,);
|
||||
addToRunTimeSelectionTable(liquid, C8H18, Istream);
|
||||
Foam::C8H18::C8H18()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
114.231,
|
||||
568.70,
|
||||
2.49e+6,
|
||||
0.486,
|
||||
0.256,
|
||||
216.38,
|
||||
2.1083,
|
||||
398.83,
|
||||
0.0,
|
||||
0.3996,
|
||||
1.54e+4
|
||||
),
|
||||
rho_(61.37745861, 0.26115, 568.7, 0.28034),
|
||||
pv_(96.084, -7900.2, -11.003, 7.1802e-06, 2.0),
|
||||
hl_(568.70, 483056.263186, 0.38467, 0.0, 0.0, 0.0),
|
||||
cp_
|
||||
(
|
||||
1968.20477803749,
|
||||
-1.63379467920267,
|
||||
0.00839448135795012,
|
||||
0.0,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-2778787.734126,
|
||||
1968.20477803749,
|
||||
-0.816897339601334,
|
||||
0.00279816045265004,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
cpg_(1186.54305748877, 3878.9820626625, 1635.6, 2673.52995246474, 746.4),
|
||||
B_
|
||||
(
|
||||
0.00239777293379205,
|
||||
-2.81394717721109,
|
||||
-585042.589139551,
|
||||
-1.11265768486663e+18,
|
||||
1.40968738783693e+20
|
||||
),
|
||||
mu_(-20.463, 1497.4, 1.379, 0.0, 0.0),
|
||||
mug_(3.1191e-08, 0.92925, 55.092, 0.0),
|
||||
K_(0.2156, -0.00029483, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(-8758, 0.8448, -27121000000.0, 0.0),
|
||||
sigma_(568.70, 0.052789, 1.2323, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 114.231, 28.0) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C8H18::C8H18
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C8H18::C8H18(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C8H18()
|
||||
:
|
||||
liquid(114.231, 568.70, 2.49e+6, 0.486, 0.256, 216.38, 2.1083, 398.83, 0.0, 0.3996, 1.54e+4),
|
||||
rho_(61.37745861, 0.26115, 568.7, 0.28034),
|
||||
pv_(96.084, -7900.2, -11.003, 7.1802e-06, 2),
|
||||
hl_(568.70, 483056.263186, 0.38467, 0, 0, 0),
|
||||
cp_(1968.20477803749, -1.63379467920267, 0.00839448135795012, 0, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-2778787.734126, 1968.20477803749, -0.816897339601334, 0.00279816045265004, 0, 0),
|
||||
cpg_(1186.54305748877, 3878.9820626625, 1635.6, 2673.52995246474, 746.4),
|
||||
B_(0.00239777293379205, -2.81394717721109, -585042.589139551, -1.11265768486663e+18, 1.40968738783693e+20),
|
||||
mu_(-20.463, 1497.4, 1.379, 0, 0),
|
||||
mug_(3.1191e-08, 0.92925, 55.092, 0),
|
||||
K_(0.2156, -0.00029483, 0, 0, 0, 0),
|
||||
Kg_(-8758, 0.8448, -27121000000.0, 0),
|
||||
sigma_(568.70, 0.052789, 1.2323, 0, 0, 0),
|
||||
D_(147.18, 20.1, 114.231, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C8H18();
|
||||
|
||||
//- Construct from components
|
||||
C8H18
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C8H18(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C8H18(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
//- Vapour pressure [Pa];
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C8H18& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C8H18I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C8H18/C8H18I.H
Normal file
105
src/thermophysicalModels/liquids/C8H18/C8H18I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C8H18::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H18::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H18::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H18::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H18::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H18::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H18::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H18::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H18::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H18::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H18::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H18::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C8H18::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "C9H20.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(C9H20, 0);
|
||||
addToRunTimeSelectionTable(liquid, C9H20,);
|
||||
addToRunTimeSelectionTable(liquid, C9H20, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(C9H20, 0);
|
||||
addToRunTimeSelectionTable(liquid, C9H20,);
|
||||
addToRunTimeSelectionTable(liquid, C9H20, Istream);
|
||||
Foam::C9H20::C9H20()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
128.258,
|
||||
594.60,
|
||||
2.29e+6,
|
||||
0.544,
|
||||
0.252,
|
||||
219.66,
|
||||
4.3058e-1,
|
||||
423.97,
|
||||
0.0,
|
||||
0.4435,
|
||||
1.56e+4
|
||||
),
|
||||
rho_(62.06019846, 0.26147, 594.6, 0.28281),
|
||||
pv_(109.35, -90304.0, -12.882, 7.8544e-06, 2.0),
|
||||
hl_(594.60, 470691.886665939, 0.38522, 0.0, 0.0, 0.0),
|
||||
cp_
|
||||
(
|
||||
2986.79224687739,
|
||||
-8.88677509395125,
|
||||
0.0211300659607978,
|
||||
0.0,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-2825628.50868792,
|
||||
2986.79224687739,
|
||||
-4.44338754697563,
|
||||
0.00704335532026592,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
cpg_(1183.16206396482, 3832.11963386299, 1644.8, 2705.48425829188, 749.6),
|
||||
B_
|
||||
(
|
||||
0.00304542406711472,
|
||||
-3.65357326638494,
|
||||
-520825.211682702,
|
||||
-6.15400208953827e+18,
|
||||
1.41901479829718e+21
|
||||
),
|
||||
mu_(-21.149, 1658, 1.454, 0.0, 0.0),
|
||||
mug_(1.0344e-07, 0.77301, 220.47, 0.0),
|
||||
K_(0.209, -0.000264, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(-0.065771, 0.27198, -3482.3, -1580300.0),
|
||||
sigma_(594.60, 0.054975, 1.2897, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 128.258, 28.0) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::C9H20::C9H20
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::C9H20::C9H20(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
C9H20()
|
||||
:
|
||||
liquid(128.258, 594.60, 2.29e+6, 0.544, 0.252, 219.66, 4.3058e-1, 423.97, 0, 0.4435, 1.56e+4),
|
||||
rho_(62.06019846, 0.26147, 594.6, 0.28281),
|
||||
pv_(109.35, -90304, -12.882, 7.8544e-06, 2),
|
||||
hl_(594.60, 470691.886665939, 0.38522, 0, 0, 0),
|
||||
cp_(2986.79224687739, -8.88677509395125, 0.0211300659607978, 0, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-2825628.50868792, 2986.79224687739, -4.44338754697563, 0.00704335532026592, 0, 0),
|
||||
cpg_(1183.16206396482, 3832.11963386299, 1644.8, 2705.48425829188, 749.6),
|
||||
B_(0.00304542406711472, -3.65357326638494, -520825.211682702, -6.15400208953827e+18, 1.41901479829718e+21),
|
||||
mu_(-21.149, 1658, 1.454, 0, 0),
|
||||
mug_(1.0344e-07, 0.77301, 220.47, 0),
|
||||
K_(0.209, -0.000264, 0, 0, 0, 0),
|
||||
Kg_(-0.065771, 0.27198, -3482.3, -1580300),
|
||||
sigma_(594.60, 0.054975, 1.2897, 0, 0, 0),
|
||||
D_(147.18, 20.1, 128.258, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
C9H20();
|
||||
|
||||
//- Construct from components
|
||||
C9H20
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
C9H20(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
C9H20(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const C9H20& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "C9H20I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/C9H20/C9H20I.H
Normal file
105
src/thermophysicalModels/liquids/C9H20/C9H20I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::C9H20::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C9H20::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C9H20::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C9H20::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C9H20::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C9H20::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C9H20::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C9H20::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C9H20::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C9H20::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C9H20::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C9H20::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::C9H20::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "CH3OH.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(CH3OH, 0);
|
||||
addToRunTimeSelectionTable(liquid, CH3OH,);
|
||||
addToRunTimeSelectionTable(liquid, CH3OH, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(CH3OH, 0);
|
||||
addToRunTimeSelectionTable(liquid, CH3OH,);
|
||||
addToRunTimeSelectionTable(liquid, CH3OH, Istream);
|
||||
Foam::CH3OH::CH3OH()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
32.042,
|
||||
512.58,
|
||||
8.0959e+6,
|
||||
0.1178,
|
||||
0.224,
|
||||
175.47,
|
||||
1.054e-1,
|
||||
337.85,
|
||||
5.6706e-30,
|
||||
0.5656,
|
||||
2.9523e+4
|
||||
),
|
||||
rho_(73.952936, 0.27192, 512.58, 0.2331),
|
||||
pv_(109.93, -7471.3, -13.988, 0.015281, 1.0),
|
||||
hl_(512.58, 1644716.30984333, 0.3766, 0.0, 0.0, 0.0),
|
||||
cp_
|
||||
(
|
||||
3358.09250358904,
|
||||
-11.8781599151114,
|
||||
0.0305536483365583,
|
||||
0.0,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-8190474.32066862,
|
||||
3358.09250358904,
|
||||
-5.93907995755571,
|
||||
0.0101845494455194,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
cpg_(1226.9521253355, 2772.92303851195, 1963, 1733.66206853505, 909.6),
|
||||
B_
|
||||
(
|
||||
-0.0199737844079645,
|
||||
19.3496036452157,
|
||||
-3342487.98452032,
|
||||
2.40808938268523e+19,
|
||||
-6.85787404032208e+21
|
||||
),
|
||||
mu_(-7.288, 1065.3, -0.6657, 0.0, 0.0),
|
||||
mug_(3.0663e-07, 0.69655, 205.0, 0.0),
|
||||
K_(0.2837, -0.000281, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(-7.763, 1.0279, -74360000.0, 6770000000.0),
|
||||
sigma_(512.58, 0.056, -0.00014583, 1.08e-07, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 32.042, 28.0) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::CH3OH::CH3OH
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::CH3OH::CH3OH(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
CH3OH()
|
||||
:
|
||||
liquid(32.042, 512.58, 8.0959e+6, 0.1178, 0.224, 175.47, 1.054e-1, 337.85, 5.6706e-30, 0.5656, 2.9523e+4),
|
||||
rho_(73.952936, 0.27192, 512.58, 0.2331),
|
||||
pv_(109.93, -7471.3, -13.988, 0.015281, 1),
|
||||
hl_(512.58, 1644716.30984333, 0.3766, 0, 0, 0),
|
||||
cp_(3358.09250358904, -11.8781599151114, 0.0305536483365583, 0, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-8190474.32066862, 3358.09250358904, -5.93907995755571, 0.0101845494455194, 0, 0),
|
||||
cpg_(1226.9521253355, 2772.92303851195, 1963, 1733.66206853505, 909.6),
|
||||
B_(-0.0199737844079645, 19.3496036452157, -3342487.98452032, 2.40808938268523e+19, -6.85787404032208e+21),
|
||||
mu_(-7.288, 1065.3, -0.6657, 0, 0),
|
||||
mug_(3.0663e-07, 0.69655, 205, 0),
|
||||
K_(0.2837, -0.000281, 0, 0, 0, 0),
|
||||
Kg_(-7.763, 1.0279, -74360000.0, 6770000000.0),
|
||||
sigma_(512.58, 0.056, -0.00014583, 1.08e-07, 0, 0),
|
||||
D_(147.18, 20.1, 32.042, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
CH3OH();
|
||||
|
||||
//- Construct from components
|
||||
CH3OH
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
CH3OH(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
CH3OH(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const CH3OH& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "CH3OHI.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/CH3OH/CH3OHI.H
Normal file
105
src/thermophysicalModels/liquids/CH3OH/CH3OHI.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::CH3OH::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH3OH::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH3OH::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH3OH::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH3OH::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH3OH::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH3OH::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH3OH::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH3OH::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH3OH::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH3OH::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH3OH::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH3OH::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -30,19 +30,108 @@ Description
|
||||
#include "CH4N2O.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(CH4N2O, 0);
|
||||
addToRunTimeSelectionTable(liquid, CH4N2O,);
|
||||
addToRunTimeSelectionTable(liquid, CH4N2O, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(CH4N2O, 0);
|
||||
addToRunTimeSelectionTable(liquid, CH4N2O,);
|
||||
addToRunTimeSelectionTable(liquid, CH4N2O, Istream);
|
||||
Foam::CH4N2O::CH4N2O()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
60.056,
|
||||
705.0,
|
||||
9.050e+6,
|
||||
0.218,
|
||||
0.337,
|
||||
405.85,
|
||||
9.3131e+1,
|
||||
465.0,
|
||||
1.52e-29,
|
||||
0.3449,
|
||||
4.7813e+4
|
||||
),
|
||||
rho_(1230.006936, 0.0, 0.0, 0.0, 0.0, 0.0),
|
||||
pv_(3015.15611544, -185497.059684, -430.223621983, 0.00017405122622, 2.0),
|
||||
hl_(705.0, 2534249.0, 0.5, 0.0, 0.0, 0.0),
|
||||
cp_(2006.46063673904, 0.0, 0.0, 0.0, 0.0, 0.0),
|
||||
h_(-6154107.41641135, 2006.46063673904, 0.0, 0.0, 0.0, 0.0),
|
||||
cpg_(811.875582789397, 2099.04089516451, 1627.3, 1603.63660583455, 724.41),
|
||||
B_
|
||||
(
|
||||
-0.000383641934194752,
|
||||
0.447249234048222,
|
||||
-469062.208605302,
|
||||
5.5628080458239e+18,
|
||||
-2.3040162514986e+21
|
||||
),
|
||||
mu_(-51.964, 3670.6, 5.7331, -5.3495e-29, 10.0),
|
||||
mug_(2.6986e-06, 0.498, 1257.7, -19570.0),
|
||||
K_(-0.4267, 0.0056903, -8.0065e-06, 1.815e-09, 0.0, 0.0),
|
||||
Kg_(6.977e-05, 1.1243, 844.9, -148850.0),
|
||||
sigma_(705.0, 1.0, 0.0, 0.0, 0.0, 0.0), // note: set to constant
|
||||
D_(147.18, 20.1, 60.056, 28.0) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::CH4N2O::CH4N2O
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc0& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::CH4N2O::CH4N2O(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -26,7 +26,8 @@ Class
|
||||
Foam::CH4N2O
|
||||
|
||||
Description
|
||||
urea, note that some of the properties are unavailable in the literature and have been copied from water.
|
||||
urea, note that some of the properties are unavailable in the literature
|
||||
and have been copied from water.
|
||||
|
||||
SourceFiles
|
||||
CH4N2O.C
|
||||
@ -86,23 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
CH4N2O()
|
||||
:
|
||||
liquid(60.056, 705.0, 9.050e+6, 0.218, 0.337, 405.85, 9.3131e+1, 465.0, 1.52e-29, 0.3449, 4.7813e+4),
|
||||
rho_(1230.006936, 0, 0, 0, 0, 0),
|
||||
pv_(3015.15611544, -185497.059684, -430.223621983, 0.00017405122622, 2.0),
|
||||
hl_(705.0, 2534249.0, 0.5, 0.0, 0.0, 0.0),
|
||||
cp_(2006.46063673904, 0, 0, 0, 0, 0),
|
||||
h_(-6154107.41641135, 2006.46063673904, 0, 0, 0, 0),
|
||||
cpg_(811.875582789397, 2099.04089516451, 1627.3, 1603.63660583455, 724.41),
|
||||
B_(-0.000383641934194752, 0.447249234048222, -469062.208605302, 5.5628080458239e+18, -2.3040162514986e+21),
|
||||
mu_(-51.964, 3670.6, 5.7331, -5.3495e-29, 10),
|
||||
mug_(2.6986e-06, 0.498, 1257.7, -19570),
|
||||
K_(-0.4267, 0.0056903, -8.0065e-06, 1.815e-09, 0, 0),
|
||||
Kg_(6.977e-05, 1.1243, 844.9, -148850),
|
||||
sigma_(705.0, 1.0, 0.0, 0.0, 0.0, 0), // set to constant
|
||||
D_(147.18, 20.1, 60.056, 28) // Same as nHeptane
|
||||
{}
|
||||
CH4N2O();
|
||||
|
||||
//- Construct from components
|
||||
CH4N2O
|
||||
(
|
||||
const liquid& l,
|
||||
@ -119,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
CH4N2O(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
CH4N2O(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -256,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const CH4N2O& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -273,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "CH4N2OI.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
106
src/thermophysicalModels/liquids/CH4N2O/CH4N2OI.H
Normal file
106
src/thermophysicalModels/liquids/CH4N2O/CH4N2OI.H
Normal file
@ -0,0 +1,106 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::CH4N2O::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH4N2O::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH4N2O::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH4N2O::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH4N2O::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH4N2O::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH4N2O::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH4N2O::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH4N2O::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH4N2O::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH4N2O::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH4N2O::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::CH4N2O::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -27,19 +27,131 @@ License
|
||||
#include "H2O.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(H2O, 0);
|
||||
addToRunTimeSelectionTable(liquid, H2O,);
|
||||
addToRunTimeSelectionTable(liquid, H2O, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(H2O, 0);
|
||||
addToRunTimeSelectionTable(liquid, H2O,);
|
||||
addToRunTimeSelectionTable(liquid, H2O, Istream);
|
||||
Foam::H2O::H2O()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
18.015,
|
||||
647.13,
|
||||
2.2055e+7,
|
||||
0.05595,
|
||||
0.229,
|
||||
273.16,
|
||||
6.113e+2,
|
||||
373.15,
|
||||
6.1709e-30,
|
||||
0.3449,
|
||||
4.7813e+4
|
||||
),
|
||||
rho_(98.343885, 0.30542, 647.13, 0.081),
|
||||
pv_(73.649, -7258.2, -7.3037, 4.1653e-06, 2),
|
||||
hl_(647.13, 2889425.47876769, 0.3199, -0.212, 0.25795, 0),
|
||||
cp_
|
||||
(
|
||||
15341.1046350264,
|
||||
-116.019983347211,
|
||||
0.451013044684985,
|
||||
-0.000783569247849015,
|
||||
5.20127671384957e-07,
|
||||
0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-17957283.7993676,
|
||||
15341.1046350264,
|
||||
-58.0099916736053,
|
||||
0.150337681561662,
|
||||
-0.000195892311962254,
|
||||
1.04025534276991e-07
|
||||
),
|
||||
cpg_
|
||||
(
|
||||
1851.73466555648,
|
||||
1487.53816264224,
|
||||
2609.3,
|
||||
493.366638912018,
|
||||
1167.6
|
||||
),
|
||||
B_
|
||||
(
|
||||
-0.0012789342214821,
|
||||
1.4909797391063,
|
||||
-1563696.91923397,
|
||||
1.85445462114904e+19,
|
||||
-7.68082153760755e+21
|
||||
),
|
||||
mu_(-51.964, 3670.6, 5.7331, -5.3495e-29, 10),
|
||||
mug_(2.6986e-06, 0.498, 1257.7, -19570),
|
||||
K_(-0.4267, 0.0056903, -8.0065e-06, 1.815e-09, 0, 0),
|
||||
Kg_(6.977e-05, 1.1243, 844.9, -148850),
|
||||
sigma_(647.13, 0.18548, 2.717, -3.554, 2.047, 0),
|
||||
D_(147.18, 20.1, 18.015, 28) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::H2O::H2O
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::H2O::H2O(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -86,26 +86,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
H2O()
|
||||
:
|
||||
liquid(18.015, 647.13, 2.2055e+7, 0.05595, 0.229, 273.16, 6.113e+2, 373.15, 6.1709e-30, 0.3449, 4.7813e+4),
|
||||
rho_(98.343885, 0.30542, 647.13, 0.081),
|
||||
pv_(73.649, -7258.2, -7.3037, 4.1653e-06, 2),
|
||||
hl_(647.13, 2889425.47876769, 0.3199, -0.212, 0.25795, 0),
|
||||
cp_(15341.1046350264, -116.019983347211, 0.451013044684985, -0.000783569247849015, 5.20127671384957e-07, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-17957283.7993676, 15341.1046350264, -58.0099916736053, 0.150337681561662, -0.000195892311962254, 1.04025534276991e-07),
|
||||
cpg_(1851.73466555648, 1487.53816264224, 2609.3, 493.366638912018, 1167.6),
|
||||
B_(-0.0012789342214821, 1.4909797391063, -1563696.91923397, 1.85445462114904e+19, -7.68082153760755e+21),
|
||||
mu_(-51.964, 3670.6, 5.7331, -5.3495e-29, 10),
|
||||
mug_(2.6986e-06, 0.498, 1257.7, -19570),
|
||||
K_(-0.4267, 0.0056903, -8.0065e-06, 1.815e-09, 0, 0),
|
||||
Kg_(6.977e-05, 1.1243, 844.9, -148850),
|
||||
sigma_(647.13, 0.18548, 2.717, -3.554, 2.047, 0),
|
||||
D_(147.18, 20.1, 18.015, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
H2O();
|
||||
|
||||
//- Construct from components
|
||||
H2O
|
||||
(
|
||||
const liquid& l,
|
||||
@ -122,125 +105,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
H2O(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
H2O(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,8 +174,7 @@ public:
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const H2O& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -276,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "H2OI.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/H2O/H2OI.H
Normal file
105
src/thermophysicalModels/liquids/H2O/H2OI.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::H2O::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::H2O::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::H2O::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::H2O::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::H2O::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::H2O::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::H2O::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::H2O::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::H2O::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::H2O::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::H2O::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::H2O::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::H2O::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,124 @@ License
|
||||
#include "IC8H18.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(IC8H18, 0);
|
||||
addToRunTimeSelectionTable(liquid, IC8H18,);
|
||||
addToRunTimeSelectionTable(liquid, IC8H18, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(IC8H18, 0);
|
||||
addToRunTimeSelectionTable(liquid, IC8H18,);
|
||||
addToRunTimeSelectionTable(liquid, IC8H18, Istream);
|
||||
Foam::IC8H18::IC8H18()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
114.231,
|
||||
543.96,
|
||||
2.5676e+6,
|
||||
0.468,
|
||||
0.266,
|
||||
165.78,
|
||||
1.4464e-2,
|
||||
372.39,
|
||||
0.0,
|
||||
0.3031,
|
||||
1.4051e+4
|
||||
),
|
||||
rho_(67.2363666, 0.27373, 543.96, 0.2846),
|
||||
pv_(120.81, -7550, -16.111, 0.017099, 1.0),
|
||||
hl_(543.96, 375379.713037617, 0.1549, 0.138, 0.0666, 0.0),
|
||||
cp_
|
||||
(
|
||||
1219.89652546156,
|
||||
1.67205049417409,
|
||||
0.00414073237562483,
|
||||
0.0,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
h_
|
||||
(
|
||||
-2743275.10767575,
|
||||
1219.89652546156,
|
||||
0.836025247087043,
|
||||
0.00138024412520828,
|
||||
0.0,
|
||||
0.0
|
||||
),
|
||||
cpg_(997.10236275617, 4627.4653990598, 1594, 2933.52942721328, 677.94),
|
||||
B_
|
||||
(
|
||||
0.00234936225718063,
|
||||
-2.83381919093766,
|
||||
-413154.047500241,
|
||||
-3.49703670632315e+17,
|
||||
3.13750207912038e+19
|
||||
),
|
||||
mu_(-15.811, 1282.5, 0.67791, -3.8617e-28, 10.0),
|
||||
mug_(1.107e-07, 0.746, 72.4, 0.0),
|
||||
K_(0.1508, -0.0001712, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(1.758e-05, 1.3114, 392.9, 0.0),
|
||||
sigma_(543.96, 0.047434, 1.1975, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 114.231, 28.0) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::IC8H18::IC8H18
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::IC8H18::IC8H18(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -87,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
IC8H18()
|
||||
:
|
||||
liquid(114.231, 543.96, 2.5676e+6, 0.468, 0.266, 165.78, 1.4464e-2, 372.39, 0.0, 0.3031, 1.4051e+4),
|
||||
rho_(67.2363666, 0.27373, 543.96, 0.2846),
|
||||
pv_(120.81, -7550, -16.111, 0.017099, 1),
|
||||
hl_(543.96, 375379.713037617, 0.1549, 0.138, 0.0666, 0),
|
||||
cp_(1219.89652546156, 1.67205049417409, 0.00414073237562483, 0, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-2743275.10767575, 1219.89652546156, 0.836025247087043, 0.00138024412520828, 0, 0),
|
||||
cpg_(997.10236275617, 4627.4653990598, 1594, 2933.52942721328, 677.94),
|
||||
B_(0.00234936225718063, -2.83381919093766, -413154.047500241, -3.49703670632315e+17, 3.13750207912038e+19),
|
||||
mu_(-15.811, 1282.5, 0.67791, -3.8617e-28, 10),
|
||||
mug_(1.107e-07, 0.746, 72.4, 0),
|
||||
K_(0.1508, -0.0001712, 0, 0, 0, 0),
|
||||
Kg_(1.758e-05, 1.3114, 392.9, 0),
|
||||
sigma_(543.96, 0.047434, 1.1975, 0, 0, 0),
|
||||
D_(147.18, 20.1, 114.231, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
IC8H18();
|
||||
|
||||
//- Construct from components
|
||||
IC8H18
|
||||
(
|
||||
const liquid& l,
|
||||
@ -123,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
IC8H18(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
IC8H18(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -260,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const IC8H18& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -277,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "IC8H18I.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/IC8H18/IC8H18I.H
Normal file
105
src/thermophysicalModels/liquids/IC8H18/IC8H18I.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::IC8H18::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IC8H18::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IC8H18::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IC8H18::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IC8H18::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IC8H18::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IC8H18::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IC8H18::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IC8H18::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IC8H18::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IC8H18::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IC8H18::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IC8H18::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,144 @@ License
|
||||
#include "IDEA.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(IDEA, 0);
|
||||
addToRunTimeSelectionTable(liquid, IDEA,);
|
||||
addToRunTimeSelectionTable(liquid, IDEA, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(IDEA, 0);
|
||||
addToRunTimeSelectionTable(liquid, IDEA,);
|
||||
addToRunTimeSelectionTable(liquid, IDEA, Istream);
|
||||
Foam::IDEA::IDEA()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
142.26,
|
||||
618.074,
|
||||
2.11e+6,
|
||||
0.523,
|
||||
0.247,
|
||||
242.67,
|
||||
3.4929e-2,
|
||||
447.3,
|
||||
1.7012e-30,
|
||||
0.3478,
|
||||
1.57e+4
|
||||
),
|
||||
rho_(152.012105, 3.87150382e-1, 618.073893, 4.00790044e-1),
|
||||
pv_
|
||||
(
|
||||
8.4817774623e+01,
|
||||
-8.6782398353e+03,
|
||||
-9.1277694857,
|
||||
4.6153144498e-06,
|
||||
2.0
|
||||
),
|
||||
hl_
|
||||
(
|
||||
618.074,
|
||||
2.1671983789e+05,
|
||||
-4.2413153435e+00,
|
||||
1.1656811532e+01,
|
||||
-1.1656446689e+01,
|
||||
4.3667661492
|
||||
),
|
||||
cp_(1.6604957e+3, -6.250871e-1, 6.1778552e-3, 0.0, 0.0, 0.0),
|
||||
h_(0.0, 0.0, 0.0, 0.0, 0.0, 0.0),
|
||||
cpg_
|
||||
(
|
||||
1.0457515243e+03,
|
||||
3.4410492875e+03,
|
||||
1.5976862298e+03,
|
||||
2.4697705752e+03,
|
||||
7.3699710536e+02
|
||||
),
|
||||
B_
|
||||
(
|
||||
0.00337351091119935,
|
||||
-4.13606494008504,
|
||||
-534560.916470464,
|
||||
-1.13364022911762e+19,
|
||||
2.80704220402713e+21
|
||||
),
|
||||
mu_(-6.9645853822e+01, 4.4390635942e+03, 8.4680722718e+00, 0.0, 0.0),
|
||||
mug_(4.2629382158e-08, 8.8144402122e-01, 9.6918097636e+01, 0.0),
|
||||
K_(2.03684e-01, -2.3168e-04, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_
|
||||
(
|
||||
-5.664925956707e+02,
|
||||
8.896721676320e-01,
|
||||
-2.849783998688e+09,
|
||||
6.914935658053e+05
|
||||
),
|
||||
sigma_
|
||||
(
|
||||
618.074,
|
||||
8.3846525429e-03,
|
||||
-1.0044759047e+01,
|
||||
2.7261918781e+01,
|
||||
-2.5529134309e+01,
|
||||
8.6488806234
|
||||
),
|
||||
D_(147.18, 20.1, 142.2, 28.0) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::IDEA::IDEA
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::IDEA::IDEA(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -109,26 +109,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
IDEA()
|
||||
:
|
||||
liquid(142.26, 618.074, 2.11e+6, 0.523, 0.247, 242.67, 3.4929e-2, 447.3, 1.7012e-30, 0.3478, 1.57e+4),
|
||||
rho_(152.012105, 3.87150382e-1, 618.073893, 4.00790044e-1),
|
||||
pv_(8.4817774623e+01, -8.6782398353e+03, -9.1277694857, 4.6153144498e-06, 2.0),
|
||||
hl_(618.074,2.1671983789e+05, -4.2413153435e+00, 1.1656811532e+01, -1.1656446689e+01, 4.3667661492),
|
||||
cp_(1.6604957e+3, -6.250871e-1, 6.1778552e-3, 0.0, 0.0, 0.0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// For this fuel I've put it to zero because I was lazy at the time...
|
||||
h_(0.0, 0.0, 0.0, 0.0, 0.0, 0.0),
|
||||
cpg_(1.0457515243e+03, 3.4410492875e+03, 1.5976862298e+03, 2.4697705752e+03, 7.3699710536e+02),
|
||||
B_(0.00337351091119935, -4.13606494008504, -534560.916470464, -1.13364022911762e+19, 2.80704220402713e+21),
|
||||
mu_(-6.9645853822e+01, 4.4390635942e+03, 8.4680722718e+00, 0.0, 0.0),
|
||||
mug_(4.2629382158e-08, 8.8144402122e-01, 9.6918097636e+01, 0.0),
|
||||
K_(2.03684e-01, -2.3168e-04, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(-5.664925956707e+02, 8.896721676320e-01, -2.849783998688e+09, 6.914935658053e+05),
|
||||
sigma_(618.074, 8.3846525429e-03, -1.0044759047e+01, 2.7261918781e+01, -2.5529134309e+01, 8.6488806234),
|
||||
D_(147.18, 20.1, 142.2, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
IDEA();
|
||||
|
||||
// Construct from components
|
||||
IDEA
|
||||
(
|
||||
const liquid& l,
|
||||
@ -145,125 +128,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
IDEA(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
IDEA(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -281,9 +195,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const IDEA& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -298,6 +210,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "IDEAI.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
105
src/thermophysicalModels/liquids/IDEA/IDEAI.H
Normal file
105
src/thermophysicalModels/liquids/IDEA/IDEAI.H
Normal file
@ -0,0 +1,105 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 1991-2009 OpenCFD Ltd.
|
||||
\\/ 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 2 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, write to the Free Software Foundation,
|
||||
Inc., 51 Franklin St, Fifth Floor, Boston, MA 02110-1301 USA
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
inline Foam::scalar Foam::IDEA::rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IDEA::pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IDEA::hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IDEA::cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IDEA::h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IDEA::cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IDEA::B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IDEA::mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IDEA::mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IDEA::K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IDEA::Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IDEA::sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
inline Foam::scalar Foam::IDEA::D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -27,19 +27,108 @@ License
|
||||
#include "MB.H"
|
||||
#include "addToRunTimeSelectionTable.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
defineTypeNameAndDebug(MB, 0);
|
||||
addToRunTimeSelectionTable(liquid, MB,);
|
||||
addToRunTimeSelectionTable(liquid, MB, Istream);
|
||||
}
|
||||
|
||||
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
|
||||
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
|
||||
|
||||
defineTypeNameAndDebug(MB, 0);
|
||||
addToRunTimeSelectionTable(liquid, MB,);
|
||||
addToRunTimeSelectionTable(liquid, MB, Istream);
|
||||
Foam::MB::MB()
|
||||
:
|
||||
liquid
|
||||
(
|
||||
102.133,
|
||||
554.5,
|
||||
3.4734e+6,
|
||||
0.34,
|
||||
0.256,
|
||||
187.35,
|
||||
1.0102e-1,
|
||||
375.90,
|
||||
5.7373e-30,
|
||||
0.3807,
|
||||
1.7713e+4
|
||||
),
|
||||
rho_(76.6099633, 0.257, 554.5, 0.2772),
|
||||
pv_(107.51, -8112.9, -12.77, 9.2919e-06, 2.0),
|
||||
hl_(554.5, 508307.794738233, 0.392, 0.0, 0.0, 0.0),
|
||||
cp_(1135.77394182096, 2.89818178257762, 0.0, 0.0, 0.0, 0.0),
|
||||
h_(-5255966.14542938, 1135.77394182096, 1.44909089128881, 0.0, 0.0, 0.0),
|
||||
cpg_(875.329227575808, 2849.22600922327, 1570.0, 2029.70636327142, 678.3),
|
||||
B_
|
||||
(
|
||||
0.00220496803188,
|
||||
-2.42184210783978,
|
||||
-401045.695318849,
|
||||
-2.85079259397061e+17,
|
||||
-3.57377145486767e+19
|
||||
),
|
||||
mu_(-12.206, 1141.7, 0.15014, 0.0, 0.0),
|
||||
mug_(3.733e-07, 0.6177, 256.5, 0.0),
|
||||
K_(0.2298, -0.0003002, 0.0, 0.0, 0.0, 0.0),
|
||||
Kg_(1333.1, 0.9962, 12317000000.0, 0.0),
|
||||
sigma_(554.5, 0.064084, 1.2418, 0.0, 0.0, 0.0),
|
||||
D_(147.18, 20.1, 102.133, 28.0) // note: Same as nHeptane
|
||||
{}
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
Foam::MB::MB
|
||||
(
|
||||
const liquid& l,
|
||||
const NSRDSfunc5& density,
|
||||
const NSRDSfunc1& vapourPressure,
|
||||
const NSRDSfunc6& heatOfVapourisation,
|
||||
const NSRDSfunc0& heatCapacity,
|
||||
const NSRDSfunc0& enthalpy,
|
||||
const NSRDSfunc7& idealGasHeatCapacity,
|
||||
const NSRDSfunc4& secondVirialCoeff,
|
||||
const NSRDSfunc1& dynamicViscosity,
|
||||
const NSRDSfunc2& vapourDynamicViscosity,
|
||||
const NSRDSfunc0& thermalConductivity,
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
|
||||
|
||||
Foam::MB::MB(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -31,8 +31,7 @@ Description
|
||||
SourceFiles
|
||||
MB.C
|
||||
|
||||
*/
|
||||
// ------------------------------------------------------------------------- //
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
#ifndef MB_H
|
||||
#define MB_H
|
||||
@ -88,26 +87,9 @@ public:
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
MB()
|
||||
:
|
||||
liquid(102.133, 554.5, 3.4734e+6, 0.34, 0.256, 187.35, 1.0102e-1, 375.90, 5.7373e-30, 0.3807, 1.7713e+4),
|
||||
rho_(76.6099633, 0.257, 554.5, 0.2772),
|
||||
pv_(107.51, -8112.9, -12.77, 9.2919e-06, 2),
|
||||
hl_(554.5, 508307.794738233, 0.392, 0, 0, 0),
|
||||
cp_(1135.77394182096, 2.89818178257762, 0, 0, 0, 0),
|
||||
// NN: enthalpy, h_, is not used in the sprayModel.
|
||||
// For consistency, the enthalpy is derived from hlat and hl.
|
||||
// It is, however, convenient to have it available.
|
||||
h_(-5255966.14542938, 1135.77394182096, 1.44909089128881, 0, 0, 0),
|
||||
cpg_(875.329227575808, 2849.22600922327, 1570, 2029.70636327142, 678.3),
|
||||
B_(0.00220496803188, -2.42184210783978, -401045.695318849, -2.85079259397061e+17, -3.57377145486767e+19),
|
||||
mu_(-12.206, 1141.7, 0.15014, 0, 0),
|
||||
mug_(3.733e-07, 0.6177, 256.5, 0),
|
||||
K_(0.2298, -0.0003002, 0, 0, 0, 0),
|
||||
Kg_(1333.1, 0.9962, 12317000000.0, 0),
|
||||
sigma_(554.5, 0.064084, 1.2418, 0, 0, 0),
|
||||
D_(147.18, 20.1, 102.133, 28) // NN: Same as nHeptane
|
||||
{}
|
||||
MB();
|
||||
|
||||
//- Construct from components
|
||||
MB
|
||||
(
|
||||
const liquid& l,
|
||||
@ -124,125 +106,56 @@ public:
|
||||
const NSRDSfunc2& vapourThermalConductivity,
|
||||
const NSRDSfunc6& surfaceTension,
|
||||
const APIdiffCoefFunc& vapourDiffussivity
|
||||
)
|
||||
:
|
||||
liquid(l),
|
||||
rho_(density),
|
||||
pv_(vapourPressure),
|
||||
hl_(heatOfVapourisation),
|
||||
cp_(heatCapacity),
|
||||
h_(enthalpy),
|
||||
cpg_(idealGasHeatCapacity),
|
||||
B_(secondVirialCoeff),
|
||||
mu_(dynamicViscosity),
|
||||
mug_(vapourDynamicViscosity),
|
||||
K_(thermalConductivity),
|
||||
Kg_(vapourThermalConductivity),
|
||||
sigma_(surfaceTension),
|
||||
D_(vapourDiffussivity)
|
||||
{}
|
||||
);
|
||||
|
||||
//- Construct from Istream
|
||||
MB(Istream& is)
|
||||
:
|
||||
liquid(is),
|
||||
rho_(is),
|
||||
pv_(is),
|
||||
hl_(is),
|
||||
cp_(is),
|
||||
h_(is),
|
||||
cpg_(is),
|
||||
B_(is),
|
||||
mu_(is),
|
||||
mug_(is),
|
||||
K_(is),
|
||||
Kg_(is),
|
||||
sigma_(is),
|
||||
D_(is)
|
||||
{}
|
||||
MB(Istream& is);
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
//- Liquid density [kg/m^3]
|
||||
scalar rho(scalar p, scalar T) const
|
||||
{
|
||||
return rho_.f(p, T);
|
||||
}
|
||||
inline scalar rho(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour pressure [Pa]
|
||||
scalar pv(scalar p, scalar T) const
|
||||
{
|
||||
return pv_.f(p, T);
|
||||
}
|
||||
inline scalar pv(scalar p, scalar T) const;
|
||||
|
||||
//- Heat of vapourisation [J/kg]
|
||||
scalar hl(scalar p, scalar T) const
|
||||
{
|
||||
return hl_.f(p, T);
|
||||
}
|
||||
inline scalar hl(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid heat capacity [J/(kg K)]
|
||||
scalar cp(scalar p, scalar T) const
|
||||
{
|
||||
return cp_.f(p, T);
|
||||
}
|
||||
inline scalar cp(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid Enthalpy [J/(kg)]
|
||||
scalar h(scalar p, scalar T) const
|
||||
{
|
||||
return h_.f(p, T);
|
||||
}
|
||||
inline scalar h(scalar p, scalar T) const;
|
||||
|
||||
//- Ideal gas heat capacity [J/(kg K)]
|
||||
scalar cpg(scalar p, scalar T) const
|
||||
{
|
||||
return cpg_.f(p, T);
|
||||
}
|
||||
inline scalar cpg(scalar p, scalar T) const;
|
||||
|
||||
//- Second Virial Coefficient [m^3/kg]
|
||||
scalar B(scalar p, scalar T) const
|
||||
{
|
||||
return B_.f(p, T);
|
||||
}
|
||||
inline scalar B(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid viscosity [Pa s]
|
||||
scalar mu(scalar p, scalar T) const
|
||||
{
|
||||
return mu_.f(p, T);
|
||||
}
|
||||
inline scalar mu(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour viscosity [Pa s]
|
||||
scalar mug(scalar p, scalar T) const
|
||||
{
|
||||
return mug_.f(p, T);
|
||||
}
|
||||
inline scalar mug(scalar p, scalar T) const;
|
||||
|
||||
//- Liquid thermal conductivity [W/(m K)]
|
||||
scalar K(scalar p, scalar T) const
|
||||
{
|
||||
return K_.f(p, T);
|
||||
}
|
||||
inline scalar K(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour thermal conductivity [W/(m K)]
|
||||
scalar Kg(scalar p, scalar T) const
|
||||
{
|
||||
return Kg_.f(p, T);
|
||||
}
|
||||
inline scalar Kg(scalar p, scalar T) const;
|
||||
|
||||
//- Surface tension [N/m]
|
||||
scalar sigma(scalar p, scalar T) const
|
||||
{
|
||||
return sigma_.f(p, T);
|
||||
}
|
||||
inline scalar sigma(scalar p, scalar T) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
scalar D(scalar p, scalar T) const
|
||||
{
|
||||
return D_.f(p, T);
|
||||
}
|
||||
inline scalar D(scalar p, scalar T) const;
|
||||
|
||||
|
||||
// I-O
|
||||
|
||||
//- Write the function coefficients
|
||||
void writeData(Ostream& os) const
|
||||
{
|
||||
@ -261,9 +174,7 @@ public:
|
||||
D_.writeData(os); os << endl;
|
||||
}
|
||||
|
||||
|
||||
// Ostream Operator
|
||||
|
||||
//- Ostream Operator
|
||||
friend Ostream& operator<<(Ostream& os, const MB& l)
|
||||
{
|
||||
l.writeData(os);
|
||||
@ -278,6 +189,10 @@ public:
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#include "MBI.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
Some files were not shown because too many files have changed in this diff Show More
Reference in New Issue
Block a user