Updated unit expressions in documentation to new standardised form
This commit is contained in:
Will Bainbridge
@ -65,7 +65,7 @@ Description
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\vartable
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\rho_c | Density of continuous phase [kg/m^3]
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\sigma | Surface tension [N/m]
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\epsilon_c | Continuous phase turbulent dissipation rate [m2/s^3]
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\epsilon_c | Continuous phase turbulent dissipation rate [m^2/s^3]
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d_i | Diameter of daughter bubble i [m]
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d_j | Diameter of mother bubble j [m]
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\endvartable
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@ -87,7 +87,7 @@ Description
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\vartable
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\alpha_c | Void fraction of continuous phase [-]
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\epsilon_c | Turbulent dissipation rate of continuous phase [m2/s^3]
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\epsilon_c | Turbulent dissipation rate of continuous phase [m^2/s^3]
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d_j | Diameter of mother bubble j [m^3]
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v_i | Volume of daughter bubble i [m^3]
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v_j | Volume of mother bubble j [m^3]
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@ -45,7 +45,7 @@ Description
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\vartable
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\sigma | Surface tension [N/m]
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v_i | Volume of mother bubble i [m]
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\epsilon_c | Turbulent dissipation rate of continuous phase [m2/s^3]
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\epsilon_c | Turbulent dissipation rate of continuous phase [m^2/s^3]
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\mu_c | Molecular dynamic viscosity of liquid phase [Pa s]
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\rho_c | Density of continuous phase [kg/m^3]
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\rho_d | Density of disperse phase [kg/m^3]
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@ -47,7 +47,7 @@ Description
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\sigma | Surface tension [N/m]
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v_i | Volume of droplet i [m^3]
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v_j | Volume of droplet j [m^3]
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\epsilon_c | Turbulent dissipation rate of continuous phase [m2/s^3]
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\epsilon_c | Turbulent dissipation rate of continuous phase [m^2/s^3]
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\alpha_d | Total void fraction of disperse phase [-]
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\mu_c | Molecular dynamic viscosity of liquid phase [Pa s]
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\rho_c | Density of continuous phase [kg/m^3]
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@ -52,14 +52,14 @@ Description
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size groups are assigned to different velocity groups.
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\vartable
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d_i | Diameter of bubble i [m]
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d_j | Diameter of bubble j [m]
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\epsilon_c | Turbulent dissipation rate of continuous phase [m2/s^3]
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\alpha | Total void fraction of the bubbles [-]
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\alpha_{max} | Maximum packing density of the bubbles [-]
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u_{crit} | Critical velocity for coalescence [m/s]
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\vec{u}_i | Velocity vector of bubble i [m/s]
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\vec{u}_j | Velocity vector of bubble j [m/s]
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d_i | Diameter of bubble i [m]
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d_j | Diameter of bubble j [m]
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\epsilon_c | Turbulent dissipation rate of continuous phase [m^2/s^3]
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\alpha | Total void fraction of the bubbles [-]
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\alpha_{max} | Maximum packing density of the bubbles [-]
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u_{crit} | Critical velocity for coalescence [m/s]
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\vec{u}_i | Velocity vector of bubble i [m/s]
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\vec{u}_j | Velocity vector of bubble j [m/s]
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\endvartable
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Reference:
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@ -64,7 +64,7 @@ Description
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C_{vm} | Virtual mass coefficient [-]
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C_1 | Coefficient [-]
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\beta | Coefficient [-]
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\epsilon_c | Continuous phase turbulent dissipation rate [m2/s^3]
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\epsilon_c | Continuous phase turbulent dissipation rate [m^2/s^3]
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\endvartable
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Reference:
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@ -83,16 +83,16 @@ Description
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is currently neglected.
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\vartable
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\theta_{ij}^{T} | Turbulent collision rate [m3/s]
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\theta_{ij}^{B} | Buoyancy-driven collision rate [m3/s]
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\theta_{ij}^{LS}| Laminar shear collision rate [m3/s]
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\theta_{ij}^{T} | Turbulent collision rate [m^3/s]
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\theta_{ij}^{B} | Buoyancy-driven collision rate [m^3/s]
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\theta_{ij}^{LS}| Laminar shear collision rate [m^3/s]
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\lambda_{ij} | Coalescence efficiency [-]
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r_{ij} | Equivalent radius [m]
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\rho_c | Density of continuous phase [kg/m^3]
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\sigma | Surface tension [N/m]
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h_0 | Initial film thickness [m]
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h_f | Critical film thickness [m]
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\epsilon_c | Continuous phase turbulent dissipation rate [m2/s^3]
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\epsilon_c | Continuous phase turbulent dissipation rate [m^2/s^3]
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d_i | Diameter of bubble i [m]
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d_j | Diameter of bubble j [m]
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u_{ri} | Rise velocity of bubble i [m/s]
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@ -46,7 +46,7 @@ Usage
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\endverbatim
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Note
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The units of kinematic turbulent thermal conductivity are [m2/s]
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The units of kinematic turbulent thermal conductivity are [m^2/s]
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See also
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Foam::fixedValueFvPatchField
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@ -43,7 +43,7 @@ Usage
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\table
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Property | Description | Required | Default value
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massFlowRate | mass flow rate [kg/s] | no |
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volumetricFlowRate | volumetric flow rate [m3/s]| no |
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volumetricFlowRate | volumetric flow rate [m^3/s]| no |
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rho | density field name | no | rho
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rhoInlet | inlet density | no |
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extrapolateProfile | Extrapolate velocity profile | no | false
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@ -39,7 +39,7 @@ Description
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U_p | velocity at the patch [m/s]
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U_c | velocity in cells adjacent to the patch [m/s]
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n | patch normal vectors
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\phi_p | flux at the patch [m3/s or kg/s]
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\phi_p | flux at the patch [m^3/s or kg/s]
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S_f | patch face area vectors [m^2]
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\endvartable
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@ -45,7 +45,7 @@ Usage
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tds | start of piston deceleration [s] | yes |
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tde | end of piston deceleration [s] | yes |
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psI | initial syringe pressure [Pa] | yes |
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psi | gas compressibility [m2/s^2] | yes |
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psi | gas compressibility [m^2/s^2] | yes |
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ams | added (or removed) gas mass [kg] | yes |
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\endtable
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@ -34,8 +34,8 @@ Description
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\f]
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where
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\vartable
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p_p | incompressible pressure at patch [m2/s^2]
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p_0 | incompressible total pressure [m2/s^2]
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p_p | incompressible pressure at patch [m^2/s^2]
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p_0 | incompressible total pressure [m^2/s^2]
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U | velocity
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\endvartable
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@ -71,7 +71,7 @@ Description
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p_p | pressure at patch [Pa]
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p_0 | total pressure [Pa]
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\gamma | ratio of specific heats (Cp/Cv)
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\psi | compressibility [m2/s^2]
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\psi | compressibility [m^2/s^2]
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G | coefficient given by \f$\frac{\gamma}{1-\gamma}\f$
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\endvartable
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@ -34,7 +34,7 @@ Description
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Usage
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\table
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Property | Description | Required | Default value
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flowRate | volumetric flow rate [m3/s] | yes |
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flowRate | volumetric flow rate [m^3/s] | yes |
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alpha | phase-fraction field | yes |
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\endtable
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@ -52,7 +52,7 @@ Description
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\rho_{\inf} | Freestream density [kg/m^3]
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p_{\inf} | Freestream pressure [Pa]
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U_{\inf} | Freestream velocity [m/s]
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p_k | Kinematic pressure (p/rho)[m2/s^2]
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p_k | Kinematic pressure (p/rho) [m^2/s^2]
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p | Pressure [Pa]
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p_0 | Total pressure [Pa]
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p_{ref} | Reference pressure level [Pa]
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@ -65,7 +65,7 @@ class COxidationDiffusionLimitedRate
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//- Stoichiometry of reaction
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const scalar Sb_;
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//- Diffusion coefficient of oxidants [m2/s]
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//- Diffusion coefficient of oxidants [m^2/s]
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const scalar D_;
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@ -154,16 +154,16 @@ Foam::scalar Foam::COxidationIntrinsicRate<CloudType>::calculate
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return 0.0;
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}
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// Diffusion rate coefficient [m2/s]
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// Diffusion rate coefficient [m^2/s]
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const scalar D0 = C1_/d*pow(0.5*(T + Tc), 0.75);
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// Apparent density of pyrolysis char [kg/m^3]
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const scalar rhop = 6.0*mass/(constant::mathematical::pi*pow3(d));
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// Knusden diffusion coefficient [m2/s]
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// Knusden diffusion coefficient [m^2/s]
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const scalar Dkn = 97.0*rMean_*sqrt(T/WO2_);
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// Effective diffusion [m2/s]
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// Effective diffusion [m^2/s]
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const scalar De = theta_/sqr(tau_)/(1.0/Dkn + 1/D0);
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// Cell carrier phase O2 species density [kg/m^3]
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@ -80,7 +80,7 @@ class COxidationIntrinsicRate
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//- Activation energy
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const scalar Ei_;
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//- Char specific internal area [m2/kg]
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//- Char specific internal area [m^2/kg]
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const scalar Ag_;
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//- Pore tortuosity []; default to sqrt(2)
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@ -83,7 +83,7 @@ class InflationInjection
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//- Injection duration [s]
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scalar duration_;
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//- Flow rate profile relative to SOI [m3/s]
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//- Flow rate profile relative to SOI [m^3/s]
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TimeFunction1<scalar> flowRateProfile_;
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//- Growth rate of particle diameters towards target [m/s]
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@ -133,7 +133,7 @@ public:
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//- Return the end-of-injection time
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scalar timeEnd() const;
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//- Return the total volumetric flow rate across the patch [m3/s]
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//- Return the total volumetric flow rate across the patch [m^3/s]
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virtual scalar flowRate() const;
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//- Number of parcels to introduce relative to SOI
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@ -173,7 +173,7 @@ void Foam::LiquidEvaporation<CloudType>::calculate
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const label gid = liqToCarrierMap_[i];
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const label lid = liqToLiqMap_[i];
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// vapour diffusivity [m2/s]
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// vapour diffusivity [m^2/s]
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const scalar Dab = liquids_.properties()[lid].D(pc, Ts);
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// saturation pressure for species i [pa]
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@ -212,7 +212,7 @@ void Foam::LiquidEvaporationBoil<CloudType>::calculate
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}
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else
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{
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// vapour diffusivity [m2/s]
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// vapour diffusivity [m^2/s]
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const scalar Dab = liquids_.properties()[lid].D(ps, Ts);
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// Schmidt number
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@ -101,7 +101,7 @@ private:
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//- Thermal conductivity [W/m/K]
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mutable thermoData kappa0_;
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//- Diffusivity [m2/s]
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//- Diffusivity [m^2/s]
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mutable thermoData D0_;
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//- Latent heat [J/kg]
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@ -169,7 +169,7 @@ public:
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//- Return thermal conductivity [W/m/K]
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virtual scalar kappa(const scalar p, const scalar T) const;
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//- Return diffusivity [m2/s]
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//- Return diffusivity [m^2/s]
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virtual scalar D(const scalar p, const scalar T) const;
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//- Return latent heat [J/kg]
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@ -130,7 +130,7 @@ public:
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//- Return thermal conductivity [W/m/K]
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virtual scalar kappa(const scalar p, const scalar T) const = 0;
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//- Return diffusivity [m2/s]
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//- Return diffusivity [m^2/s]
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virtual scalar D(const scalar p, const scalar T) const = 0;
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//- Return latent heat [J/kg]
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@ -136,7 +136,7 @@ public:
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//- Return thermal conductivity [W/m/K]
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virtual scalar kappa(const scalar p, const scalar T) const;
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//- Return diffusivity [m2/s]
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//- Return diffusivity [m^2/s]
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virtual scalar D(const scalar p, const scalar T) const;
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//- Return latent heat [J/kg]
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@ -173,7 +173,7 @@ void standardPhaseChange::correctModel
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// Vapour mass fraction at interface
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const scalar Ys = Wliq*pSat/(Wliq*pSat + Wvap*(pc - pSat));
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// Vapour diffusivity [m2/s]
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// Vapour diffusivity [m^2/s]
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const scalar Dab = filmThermo.D(pc, Tloc);
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// Schmidt number
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@ -274,7 +274,7 @@ void waxSolventEvaporation::correctModel
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// Reynolds number
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const scalar Re = rhoInfc*mag(dU[celli])*L_/muInfc;
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// Vapour diffusivity [m2/s]
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// Vapour diffusivity [m^2/s]
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const scalar Dab = filmThermo.D(pc, Tloc);
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// Schmidt number
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@ -157,10 +157,10 @@ public:
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//- Surface tension [N/m]
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inline scalar sigma(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s]
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//- Vapour diffussivity [m^2/s]
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inline scalar D(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s] with specified binary pair
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//- Vapour diffussivity [m^2/s] with specified binary pair
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inline scalar D(scalar p, scalar T, scalar Wb) const;
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@ -157,10 +157,10 @@ public:
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//- Surface tension [N/m]
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inline scalar sigma(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s]
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//- Vapour diffussivity [m^2/s]
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inline scalar D(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s] with specified binary pair
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//- Vapour diffussivity [m^2/s] with specified binary pair
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inline scalar D(scalar p, scalar T, scalar Wb) const;
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@ -157,10 +157,10 @@ public:
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//- Surface tension [N/m]
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inline scalar sigma(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s]
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//- Vapour diffussivity [m^2/s]
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inline scalar D(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s] with specified binary pair
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//- Vapour diffussivity [m^2/s] with specified binary pair
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inline scalar D(scalar p, scalar T, scalar Wb) const;
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@ -157,10 +157,10 @@ public:
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//- Surface tension [N/m]
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inline scalar sigma(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s]
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//- Vapour diffussivity [m^2/s]
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inline scalar D(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s] with specified binary pair
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//- Vapour diffussivity [m^2/s] with specified binary pair
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inline scalar D(scalar p, scalar T, scalar Wb) const;
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@ -157,10 +157,10 @@ public:
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//- Surface tension [N/m]
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inline scalar sigma(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s]
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//- Vapour diffussivity [m^2/s]
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inline scalar D(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s] with specified binary pair
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//- Vapour diffussivity [m^2/s] with specified binary pair
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inline scalar D(scalar p, scalar T, scalar Wb) const;
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@ -157,10 +157,10 @@ public:
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//- Surface tension [N/m]
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inline scalar sigma(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s]
|
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//- Vapour diffussivity [m^2/s]
|
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inline scalar D(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s] with specified binary pair
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//- Vapour diffussivity [m^2/s] with specified binary pair
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inline scalar D(scalar p, scalar T, scalar Wb) const;
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@ -157,10 +157,10 @@ public:
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//- Surface tension [N/m]
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inline scalar sigma(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s]
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//- Vapour diffussivity [m^2/s]
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inline scalar D(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s] with specified binary pair
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//- Vapour diffussivity [m^2/s] with specified binary pair
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inline scalar D(scalar p, scalar T, scalar Wb) const;
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@ -157,10 +157,10 @@ public:
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//- Surface tension [N/m]
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inline scalar sigma(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s]
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//- Vapour diffussivity [m^2/s]
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inline scalar D(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s] with specified binary pair
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//- Vapour diffussivity [m^2/s] with specified binary pair
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inline scalar D(scalar p, scalar T, scalar Wb) const;
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@ -157,10 +157,10 @@ public:
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//- Surface tension [N/m]
|
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inline scalar sigma(scalar p, scalar T) const;
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//- Vapour diffussivity [m2/s]
|
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//- Vapour diffussivity [m^2/s]
|
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inline scalar D(scalar p, scalar T) const;
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|
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//- Vapour diffussivity [m2/s] with specified binary pair
|
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//- Vapour diffussivity [m^2/s] with specified binary pair
|
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inline scalar D(scalar p, scalar T, scalar Wb) const;
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|
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|
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@ -157,10 +157,10 @@ public:
|
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//- Surface tension [N/m]
|
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inline scalar sigma(scalar p, scalar T) const;
|
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|
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//- Vapour diffussivity [m2/s]
|
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//- Vapour diffussivity [m^2/s]
|
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inline scalar D(scalar p, scalar T) const;
|
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|
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//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -156,10 +156,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -156,10 +156,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -179,10 +179,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -157,10 +157,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
|
||||
|
||||
@ -155,10 +155,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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)
|
||||
inline scalar D(scalar p, scalar T, scalar Wb) const;
|
||||
|
||||
|
||||
@ -225,7 +225,7 @@ public:
|
||||
const scalarField& X
|
||||
) const;
|
||||
|
||||
//- Vapour diffussivity [m2/s]
|
||||
//- Vapour diffussivity [m^2/s]
|
||||
scalar D
|
||||
(
|
||||
const scalar p,
|
||||
|
||||
@ -259,10 +259,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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;
|
||||
|
||||
//- Invert the vapour pressure relationship to retrieve the
|
||||
|
||||
@ -155,10 +155,10 @@ public:
|
||||
//- Surface tension [N/m]
|
||||
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;
|
||||
|
||||
//- 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)
|
||||
inline scalar D(scalar p, scalar T, scalar Wb) const;
|
||||
|
||||
|
||||
Reference in New Issue
Block a user