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Updated unit expressions in documentation to new standardised form

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This commit is contained in:
Will Bainbridge
2019-07-08 16:04:10 +01:00
parent 9cc193398f
commit 3431c1d21e
58 changed files with 104 additions and 104 deletions
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2
applications/solvers/multiphase/reactingEulerFoam/phaseSystems/populationBalanceModel/binaryBreakupModels/LehrMilliesMewes/LehrMilliesMewes.H
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@ -65,7 +65,7 @@ Description
\vartable \vartable
\rho_c | Density of continuous phase [kg/m^3] \rho_c | Density of continuous phase [kg/m^3]
\sigma | Surface tension [N/m] \sigma | Surface tension [N/m]
\epsilon_c | Continuous phase turbulent dissipation rate [m2/s^3] \epsilon_c | Continuous phase turbulent dissipation rate [m^2/s^3]
d_i | Diameter of daughter bubble i [m] d_i | Diameter of daughter bubble i [m]
d_j | Diameter of mother bubble j [m] d_j | Diameter of mother bubble j [m]
\endvartable \endvartable

2
applications/solvers/multiphase/reactingEulerFoam/phaseSystems/populationBalanceModel/binaryBreakupModels/LuoSvendsen/LuoSvendsen.H
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@ -87,7 +87,7 @@ Description
\vartable \vartable
\alpha_c | Void fraction of continuous phase [-] \alpha_c | Void fraction of continuous phase [-]
\epsilon_c | Turbulent dissipation rate of continuous phase [m2/s^3] \epsilon_c | Turbulent dissipation rate of continuous phase [m^2/s^3]
d_j | Diameter of mother bubble j [m^3] d_j | Diameter of mother bubble j [m^3]
v_i | Volume of daughter bubble i [m^3] v_i | Volume of daughter bubble i [m^3]
v_j | Volume of mother bubble j [m^3] v_j | Volume of mother bubble j [m^3]

2
applications/solvers/multiphase/reactingEulerFoam/phaseSystems/populationBalanceModel/breakupModels/LaakkonenAlopaeusAittamaa/LaakkonenAlopaeusAittamaa.H
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@ -45,7 +45,7 @@ Description
\vartable \vartable
\sigma | Surface tension [N/m] \sigma | Surface tension [N/m]
v_i | Volume of mother bubble i [m] v_i | Volume of mother bubble i [m]
\epsilon_c | Turbulent dissipation rate of continuous phase [m2/s^3] \epsilon_c | Turbulent dissipation rate of continuous phase [m^2/s^3]
\mu_c | Molecular dynamic viscosity of liquid phase [Pa s] \mu_c | Molecular dynamic viscosity of liquid phase [Pa s]
\rho_c | Density of continuous phase [kg/m^3] \rho_c | Density of continuous phase [kg/m^3]
\rho_d | Density of disperse phase [kg/m^3] \rho_d | Density of disperse phase [kg/m^3]

2
applications/solvers/multiphase/reactingEulerFoam/phaseSystems/populationBalanceModel/coalescenceModels/CoulaloglouTavlaridesCoalescence/CoulaloglouTavlaridesCoalescence.H
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@ -47,7 +47,7 @@ Description
\sigma | Surface tension [N/m] \sigma | Surface tension [N/m]
v_i | Volume of droplet i [m^3] v_i | Volume of droplet i [m^3]
v_j | Volume of droplet j [m^3] v_j | Volume of droplet j [m^3]
\epsilon_c | Turbulent dissipation rate of continuous phase [m2/s^3] \epsilon_c | Turbulent dissipation rate of continuous phase [m^2/s^3]
\alpha_d | Total void fraction of disperse phase [-] \alpha_d | Total void fraction of disperse phase [-]
\mu_c | Molecular dynamic viscosity of liquid phase [Pa s] \mu_c | Molecular dynamic viscosity of liquid phase [Pa s]
\rho_c | Density of continuous phase [kg/m^3] \rho_c | Density of continuous phase [kg/m^3]

16
applications/solvers/multiphase/reactingEulerFoam/phaseSystems/populationBalanceModel/coalescenceModels/LehrMilliesMewesCoalescence/LehrMilliesMewesCoalescence.H
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@ -52,14 +52,14 @@ Description
size groups are assigned to different velocity groups. size groups are assigned to different velocity groups.
\vartable \vartable
d_i | Diameter of bubble i [m] d_i | Diameter of bubble i [m]
d_j | Diameter of bubble j [m] d_j | Diameter of bubble j [m]
\epsilon_c | Turbulent dissipation rate of continuous phase [m2/s^3] \epsilon_c | Turbulent dissipation rate of continuous phase [m^2/s^3]
\alpha | Total void fraction of the bubbles [-] \alpha | Total void fraction of the bubbles [-]
\alpha_{max} | Maximum packing density of the bubbles [-] \alpha_{max} | Maximum packing density of the bubbles [-]
u_{crit} | Critical velocity for coalescence [m/s] u_{crit} | Critical velocity for coalescence [m/s]
\vec{u}_i | Velocity vector of bubble i [m/s] \vec{u}_i | Velocity vector of bubble i [m/s]
\vec{u}_j | Velocity vector of bubble j [m/s] \vec{u}_j | Velocity vector of bubble j [m/s]
\endvartable \endvartable
Reference: Reference:

2
applications/solvers/multiphase/reactingEulerFoam/phaseSystems/populationBalanceModel/coalescenceModels/Luo/Luo.H
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@ -64,7 +64,7 @@ Description
C_{vm} | Virtual mass coefficient [-] C_{vm} | Virtual mass coefficient [-]
C_1 | Coefficient [-] C_1 | Coefficient [-]
\beta | Coefficient [-] \beta | Coefficient [-]
\epsilon_c | Continuous phase turbulent dissipation rate [m2/s^3] \epsilon_c | Continuous phase turbulent dissipation rate [m^2/s^3]
\endvartable \endvartable
Reference: Reference:

8
applications/solvers/multiphase/reactingEulerFoam/phaseSystems/populationBalanceModel/coalescenceModels/PrinceBlanch/PrinceBlanch.H
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@ -83,16 +83,16 @@ Description
is currently neglected. is currently neglected.
\vartable \vartable
\theta_{ij}^{T} | Turbulent collision rate [m3/s] \theta_{ij}^{T} | Turbulent collision rate [m^3/s]
\theta_{ij}^{B} | Buoyancy-driven collision rate [m3/s] \theta_{ij}^{B} | Buoyancy-driven collision rate [m^3/s]
\theta_{ij}^{LS}| Laminar shear collision rate [m3/s] \theta_{ij}^{LS}| Laminar shear collision rate [m^3/s]
\lambda_{ij} | Coalescence efficiency [-] \lambda_{ij} | Coalescence efficiency [-]
r_{ij} | Equivalent radius [m] r_{ij} | Equivalent radius [m]
\rho_c | Density of continuous phase [kg/m^3] \rho_c | Density of continuous phase [kg/m^3]
\sigma | Surface tension [N/m] \sigma | Surface tension [N/m]
h_0 | Initial film thickness [m] h_0 | Initial film thickness [m]
h_f | Critical film thickness [m] h_f | Critical film thickness [m]
\epsilon_c | Continuous phase turbulent dissipation rate [m2/s^3] \epsilon_c | Continuous phase turbulent dissipation rate [m^2/s^3]
d_i | Diameter of bubble i [m] d_i | Diameter of bubble i [m]
d_j | Diameter of bubble j [m] d_j | Diameter of bubble j [m]
u_{ri} | Rise velocity of bubble i [m/s] u_{ri} | Rise velocity of bubble i [m/s]

2
src/TurbulenceModels/incompressible/turbulentTransportModels/derivedFvPatchFields/wallFunctions/alphatWallFunctions/alphatJayatillekeWallFunction/alphatJayatillekeWallFunctionFvPatchScalarField.H
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@ -46,7 +46,7 @@ Usage
\endverbatim \endverbatim
Note Note
The units of kinematic turbulent thermal conductivity are [m2/s] The units of kinematic turbulent thermal conductivity are [m^2/s]
See also See also
Foam::fixedValueFvPatchField Foam::fixedValueFvPatchField

2
src/finiteVolume/fields/fvPatchFields/derived/flowRateInletVelocity/flowRateInletVelocityFvPatchVectorField.H
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@ -43,7 +43,7 @@ Usage
\table \table
Property | Description | Required | Default value Property | Description | Required | Default value
massFlowRate | mass flow rate [kg/s] | no | massFlowRate | mass flow rate [kg/s] | no |
volumetricFlowRate | volumetric flow rate [m3/s]| no | volumetricFlowRate | volumetric flow rate [m^3/s]| no |
rho | density field name | no | rho rho | density field name | no | rho
rhoInlet | inlet density | no | rhoInlet | inlet density | no |
extrapolateProfile | Extrapolate velocity profile | no | false extrapolateProfile | Extrapolate velocity profile | no | false

2
src/finiteVolume/fields/fvPatchFields/derived/fluxCorrectedVelocity/fluxCorrectedVelocityFvPatchVectorField.H
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@ -39,7 +39,7 @@ Description
U_p | velocity at the patch [m/s] U_p | velocity at the patch [m/s]
U_c | velocity in cells adjacent to the patch [m/s] U_c | velocity in cells adjacent to the patch [m/s]
n | patch normal vectors n | patch normal vectors
\phi_p | flux at the patch [m3/s or kg/s] \phi_p | flux at the patch [m^3/s or kg/s]
S_f | patch face area vectors [m^2] S_f | patch face area vectors [m^2]
\endvartable \endvartable

2
src/finiteVolume/fields/fvPatchFields/derived/syringePressure/syringePressureFvPatchScalarField.H
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@ -45,7 +45,7 @@ Usage
tds | start of piston deceleration [s] | yes | tds | start of piston deceleration [s] | yes |
tde | end of piston deceleration [s] | yes | tde | end of piston deceleration [s] | yes |
psI | initial syringe pressure [Pa] | yes | psI | initial syringe pressure [Pa] | yes |
psi | gas compressibility [m2/s^2] | yes | psi | gas compressibility [m^2/s^2] | yes |
ams | added (or removed) gas mass [kg] | yes | ams | added (or removed) gas mass [kg] | yes |
\endtable \endtable

6
src/finiteVolume/fields/fvPatchFields/derived/totalPressure/totalPressureFvPatchScalarField.H
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@ -34,8 +34,8 @@ Description
\f] \f]
where where
\vartable \vartable
p_p | incompressible pressure at patch [m2/s^2] p_p | incompressible pressure at patch [m^2/s^2]
p_0 | incompressible total pressure [m2/s^2] p_0 | incompressible total pressure [m^2/s^2]
U | velocity U | velocity
\endvartable \endvartable
@ -71,7 +71,7 @@ Description
p_p | pressure at patch [Pa] p_p | pressure at patch [Pa]
p_0 | total pressure [Pa] p_0 | total pressure [Pa]
\gamma | ratio of specific heats (Cp/Cv) \gamma | ratio of specific heats (Cp/Cv)
\psi | compressibility [m2/s^2] \psi | compressibility [m^2/s^2]
G | coefficient given by \f$\frac{\gamma}{1-\gamma}\f$ G | coefficient given by \f$\frac{\gamma}{1-\gamma}\f$
\endvartable \endvartable

2
src/finiteVolume/fields/fvPatchFields/derived/variableHeightFlowRateInletVelocity/variableHeightFlowRateInletVelocityFvPatchVectorField.H
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@ -34,7 +34,7 @@ Description
Usage Usage
\table \table
Property | Description | Required | Default value Property | Description | Required | Default value
flowRate | volumetric flow rate [m3/s] | yes | flowRate | volumetric flow rate [m^3/s] | yes |
alpha | phase-fraction field | yes | alpha | phase-fraction field | yes |
\endtable \endtable

2
src/functionObjects/field/pressure/pressure.H
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@ -52,7 +52,7 @@ Description
\rho_{\inf} | Freestream density [kg/m^3] \rho_{\inf} | Freestream density [kg/m^3]
p_{\inf} | Freestream pressure [Pa] p_{\inf} | Freestream pressure [Pa]
U_{\inf} | Freestream velocity [m/s] U_{\inf} | Freestream velocity [m/s]
p_k | Kinematic pressure (p/rho)[m2/s^2] p_k | Kinematic pressure (p/rho) [m^2/s^2]
p | Pressure [Pa] p | Pressure [Pa]
p_0 | Total pressure [Pa] p_0 | Total pressure [Pa]
p_{ref} | Reference pressure level [Pa] p_{ref} | Reference pressure level [Pa]

2
src/lagrangian/coalCombustion/submodels/surfaceReactionModel/COxidationDiffusionLimitedRate/COxidationDiffusionLimitedRate.H
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@ -65,7 +65,7 @@ class COxidationDiffusionLimitedRate
//- Stoichiometry of reaction //- Stoichiometry of reaction
const scalar Sb_; const scalar Sb_;
//- Diffusion coefficient of oxidants [m2/s] //- Diffusion coefficient of oxidants [m^2/s]
const scalar D_; const scalar D_;

6
src/lagrangian/coalCombustion/submodels/surfaceReactionModel/COxidationIntrinsicRate/COxidationIntrinsicRate.C
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@ -154,16 +154,16 @@ Foam::scalar Foam::COxidationIntrinsicRate<CloudType>::calculate
return 0.0; return 0.0;
} }
// Diffusion rate coefficient [m2/s] // Diffusion rate coefficient [m^2/s]
const scalar D0 = C1_/d*pow(0.5*(T + Tc), 0.75); const scalar D0 = C1_/d*pow(0.5*(T + Tc), 0.75);
// Apparent density of pyrolysis char [kg/m^3] // Apparent density of pyrolysis char [kg/m^3]
const scalar rhop = 6.0*mass/(constant::mathematical::pi*pow3(d)); const scalar rhop = 6.0*mass/(constant::mathematical::pi*pow3(d));
// Knusden diffusion coefficient [m2/s] // Knusden diffusion coefficient [m^2/s]
const scalar Dkn = 97.0*rMean_*sqrt(T/WO2_); const scalar Dkn = 97.0*rMean_*sqrt(T/WO2_);
// Effective diffusion [m2/s] // Effective diffusion [m^2/s]
const scalar De = theta_/sqr(tau_)/(1.0/Dkn + 1/D0); const scalar De = theta_/sqr(tau_)/(1.0/Dkn + 1/D0);
// Cell carrier phase O2 species density [kg/m^3] // Cell carrier phase O2 species density [kg/m^3]

2
src/lagrangian/coalCombustion/submodels/surfaceReactionModel/COxidationIntrinsicRate/COxidationIntrinsicRate.H
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@ -80,7 +80,7 @@ class COxidationIntrinsicRate
//- Activation energy //- Activation energy
const scalar Ei_; const scalar Ei_;
//- Char specific internal area [m2/kg] //- Char specific internal area [m^2/kg]
const scalar Ag_; const scalar Ag_;
//- Pore tortuosity []; default to sqrt(2) //- Pore tortuosity []; default to sqrt(2)

2
src/lagrangian/intermediate/submodels/Kinematic/InjectionModel/InflationInjection/InflationInjection.H
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@ -83,7 +83,7 @@ class InflationInjection
//- Injection duration [s] //- Injection duration [s]
scalar duration_; scalar duration_;
//- Flow rate profile relative to SOI [m3/s] //- Flow rate profile relative to SOI [m^3/s]
TimeFunction1<scalar> flowRateProfile_; TimeFunction1<scalar> flowRateProfile_;
//- Growth rate of particle diameters towards target [m/s] //- Growth rate of particle diameters towards target [m/s]

2
src/lagrangian/intermediate/submodels/Kinematic/InjectionModel/PatchFlowRateInjection/PatchFlowRateInjection.H
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@ -133,7 +133,7 @@ public:
//- Return the end-of-injection time //- Return the end-of-injection time
scalar timeEnd() const; scalar timeEnd() const;
//- Return the total volumetric flow rate across the patch [m3/s] //- Return the total volumetric flow rate across the patch [m^3/s]
virtual scalar flowRate() const; virtual scalar flowRate() const;
//- Number of parcels to introduce relative to SOI //- Number of parcels to introduce relative to SOI

2
src/lagrangian/intermediate/submodels/Reacting/PhaseChangeModel/LiquidEvaporation/LiquidEvaporation.C
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@ -173,7 +173,7 @@ void Foam::LiquidEvaporation<CloudType>::calculate
const label gid = liqToCarrierMap_[i]; const label gid = liqToCarrierMap_[i];
const label lid = liqToLiqMap_[i]; const label lid = liqToLiqMap_[i];
// vapour diffusivity [m2/s] // vapour diffusivity [m^2/s]
const scalar Dab = liquids_.properties()[lid].D(pc, Ts); const scalar Dab = liquids_.properties()[lid].D(pc, Ts);
// saturation pressure for species i [pa] // saturation pressure for species i [pa]

2
src/lagrangian/intermediate/submodels/Reacting/PhaseChangeModel/LiquidEvaporationBoil/LiquidEvaporationBoil.C
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@ -212,7 +212,7 @@ void Foam::LiquidEvaporationBoil<CloudType>::calculate
} }
else else
{ {
// vapour diffusivity [m2/s] // vapour diffusivity [m^2/s]
const scalar Dab = liquids_.properties()[lid].D(ps, Ts); const scalar Dab = liquids_.properties()[lid].D(ps, Ts);
// Schmidt number // Schmidt number

4
src/regionModels/surfaceFilmModels/submodels/kinematic/filmThermoModel/constantFilmThermo/constantFilmThermo.H
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@ -101,7 +101,7 @@ private:
//- Thermal conductivity [W/m/K] //- Thermal conductivity [W/m/K]
mutable thermoData kappa0_; mutable thermoData kappa0_;
//- Diffusivity [m2/s] //- Diffusivity [m^2/s]
mutable thermoData D0_; mutable thermoData D0_;
//- Latent heat [J/kg] //- Latent heat [J/kg]
@ -169,7 +169,7 @@ public:
//- Return thermal conductivity [W/m/K] //- Return thermal conductivity [W/m/K]
virtual scalar kappa(const scalar p, const scalar T) const; virtual scalar kappa(const scalar p, const scalar T) const;
//- Return diffusivity [m2/s] //- Return diffusivity [m^2/s]
virtual scalar D(const scalar p, const scalar T) const; virtual scalar D(const scalar p, const scalar T) const;
//- Return latent heat [J/kg] //- Return latent heat [J/kg]

2
src/regionModels/surfaceFilmModels/submodels/kinematic/filmThermoModel/filmThermoModel/filmThermoModel.H
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@ -130,7 +130,7 @@ public:
//- Return thermal conductivity [W/m/K] //- Return thermal conductivity [W/m/K]
virtual scalar kappa(const scalar p, const scalar T) const = 0; virtual scalar kappa(const scalar p, const scalar T) const = 0;
//- Return diffusivity [m2/s] //- Return diffusivity [m^2/s]
virtual scalar D(const scalar p, const scalar T) const = 0; virtual scalar D(const scalar p, const scalar T) const = 0;
//- Return latent heat [J/kg] //- Return latent heat [J/kg]

2
src/regionModels/surfaceFilmModels/submodels/kinematic/filmThermoModel/liquidFilmThermo/liquidFilmThermo.H
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@ -136,7 +136,7 @@ public:
//- Return thermal conductivity [W/m/K] //- Return thermal conductivity [W/m/K]
virtual scalar kappa(const scalar p, const scalar T) const; virtual scalar kappa(const scalar p, const scalar T) const;
//- Return diffusivity [m2/s] //- Return diffusivity [m^2/s]
virtual scalar D(const scalar p, const scalar T) const; virtual scalar D(const scalar p, const scalar T) const;
//- Return latent heat [J/kg] //- Return latent heat [J/kg]

2
src/regionModels/surfaceFilmModels/submodels/thermo/phaseChangeModel/standardPhaseChange/standardPhaseChange.C
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@ -173,7 +173,7 @@ void standardPhaseChange::correctModel
// Vapour mass fraction at interface // Vapour mass fraction at interface
const scalar Ys = Wliq*pSat/(Wliq*pSat + Wvap*(pc - pSat)); const scalar Ys = Wliq*pSat/(Wliq*pSat + Wvap*(pc - pSat));
// Vapour diffusivity [m2/s] // Vapour diffusivity [m^2/s]
const scalar Dab = filmThermo.D(pc, Tloc); const scalar Dab = filmThermo.D(pc, Tloc);
// Schmidt number // Schmidt number

2
src/regionModels/surfaceFilmModels/submodels/thermo/phaseChangeModel/waxSolventEvaporation/waxSolventEvaporation.C
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@ -274,7 +274,7 @@ void waxSolventEvaporation::correctModel
// Reynolds number // Reynolds number
const scalar Re = rhoInfc*mag(dU[celli])*L_/muInfc; const scalar Re = rhoInfc*mag(dU[celli])*L_/muInfc;
// Vapour diffusivity [m2/s] // Vapour diffusivity [m^2/s]
const scalar Dab = filmThermo.D(pc, Tloc); const scalar Dab = filmThermo.D(pc, Tloc);
// Schmidt number // Schmidt number

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/Ar/Ar.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C10H22/C10H22.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C12H26/C12H26.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C13H28/C13H28.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C14H30/C14H30.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C16H34/C16H34.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C2H5OH/C2H5OH.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C2H6/C2H6.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C2H6O/C2H6O.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C3H6O/C3H6O.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C3H8/C3H8.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C4H10O/C4H10O.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C6H14/C6H14.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C6H6/C6H6.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C7H16/C7H16.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C7H8/C7H8.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C8H10/C8H10.H
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@ -156,10 +156,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C8H18/C8H18.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/C9H20/C9H20.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/CH3OH/CH3OH.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/CH4N2O/CH4N2O.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/H2O/H2O.H
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@ -156,10 +156,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/IC8H18/IC8H18.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/IDEA/IDEA.H
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@ -179,10 +179,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/MB/MB.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/N2/N2.H
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@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/aC10H7CH3/aC10H7CH3.H
View File

@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/bC10H7CH3/bC10H7CH3.H
View File

@ -157,10 +157,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/iC3H8O/iC3H8O.H
View File

@ -155,10 +155,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
// Note: behaves the same as D(p, T) // Note: behaves the same as D(p, T)
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;

2
src/thermophysicalModels/thermophysicalProperties/liquidProperties/liquidMixtureProperties/liquidMixtureProperties.H
View File

@ -225,7 +225,7 @@ public:
const scalarField& X const scalarField& X
) const; ) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
scalar D scalar D
( (
const scalar p, const scalar p,

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/liquidProperties/liquidProperties.H
View File

@ -259,10 +259,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
virtual scalar sigma(scalar p, scalar T) const = 0; virtual scalar sigma(scalar p, scalar T) const = 0;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
virtual scalar D(scalar p, scalar T) const = 0; virtual scalar D(scalar p, scalar T) const = 0;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
virtual scalar D(scalar p, scalar T, scalar Wb) const = 0; virtual scalar D(scalar p, scalar T, scalar Wb) const = 0;
//- Invert the vapour pressure relationship to retrieve the //- Invert the vapour pressure relationship to retrieve the

4
src/thermophysicalModels/thermophysicalProperties/liquidProperties/nC3H8O/nC3H8O.H
View File

@ -155,10 +155,10 @@ public:
//- Surface tension [N/m] //- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const; inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] //- Vapour diffussivity [m^2/s]
inline scalar D(scalar p, scalar T) const; inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair //- Vapour diffussivity [m^2/s] with specified binary pair
// Note: behaves the same as D(p, T) // Note: behaves the same as D(p, T)
inline scalar D(scalar p, scalar T, scalar Wb) const; inline scalar D(scalar p, scalar T, scalar Wb) const;