sunfluidh:fluid_properties_examples
Différences
Ci-dessous, les différences entre deux révisions de la page.
Les deux révisions précédentesRévision précédenteProchaine révision | Révision précédente | ||
sunfluidh:fluid_properties_examples [2016/11/18 10:20] – [Low Mach-number Flows (perfect gas only)] yann | sunfluidh:fluid_properties_examples [2016/11/29 14:58] (Version actuelle) – yann | ||
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- | ==== Examples of data set related to the namelist " | + | ===== Examples of data set ===== |
- | The user finds here some examples illustrating different configurations related to the namelist [[sunfluidh: | + | The user finds here some examples illustrating different configurations related to the namelist [[sunfluidh: |
- | Data values are showed for equations used in dimensional form.\\ | + | The data initialized by default, and not explicitly required, are generally not present for a sake of clarity.\\ |
+ | Data values are showed for equations used in a dimensional form.\\ | ||
- | ==== Monophasic | + | ----- |
+ | ==== Usual incompressible Flows ==== | ||
- | === Without heat transfer | + | ----- |
+ | <WRAP info> | ||
+ | One fluid is considered.\\ | ||
+ | In these examples, the physical properties are constant but the viscosity or the thermal conductivity can depend on temperature (Sutherland' | ||
+ | The heat capacity of the fluid is considered constant(no temperature dependence).\\ | ||
+ | The gravity or buoyancy effects are related to the temperature variation only.\\ | ||
+ | </ | ||
+ | === Isothermal flows === | ||
& | & | ||
Reference_Density | Reference_Density | ||
+ | === Example of axisymmetrical flows === | ||
- | === With heat transfer and buoyancy force === | + | & |
+ | | ||
+ | | ||
- | | + | <note important> |
+ | |||
+ | |||
+ | === Flows with Boussinesq' | ||
+ | < | ||
+ | Here Heat transfer are considered.\\ | ||
+ | The physical properties are constant.\\ | ||
+ | The buoyancy effect are related to the temperature variation.\\ | ||
+ | </ | ||
+ | | ||
+ | Reference_Dynamic_Viscosity = 1.84D-05 , | ||
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- | Note: For incompressible flows with buoyancy | + | <note important> |
+ | Don not forget also to define the gravity constant in the namelist [[sunfluidh: | ||
Thermal_Expansion_Coefficient= 0.0 involves that it is automatically calculated as the inverse of the " | Thermal_Expansion_Coefficient= 0.0 involves that it is automatically calculated as the inverse of the " | ||
The " | The " | ||
- | In these cases, the equation of enthalpy is globally considered and not its simplified version that leads to the equation of temperature. | + | In these cases, the equation of enthalpy is globally considered and not its simplified version that leads to the equation of temperature.</note> |
- | + | ||
- | === Example of Axisymmetric flows === | + | |
- | + | ||
- | & | + | |
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- | Note : In this case, do not forget to define the domain in cylindrical geometry (see the Namelist [[sunfluidh: | + | |
- | + | ||
- | ==== Incompressible two phase flows without heat transfer (physical properties of each fluid is constant) ==== | + | |
+ | ----- | ||
+ | ==== Incompressible two phase flows ==== | ||
+ | ----- | ||
+ | <WRAP info> | ||
+ | No heat transfer is considered at present.\\ | ||
+ | The physical properties of each fluid are constant.\\ | ||
+ | Two-phase flow simulations are performed with a level approach.\\ | ||
+ | The simulations are restricted to enclosed domains at present.\\ | ||
+ | </ | ||
& | & | ||
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<note important> | <note important> | ||
- | Note : " | + | " |
- | + | ----- | |
- | ==== Low Mach-number Flows (perfect gas only) ==== | + | ==== Low Mach-number Flows ==== |
- | + | ----- | |
- | === Flows with heat transfer | + | <WRAP info> |
+ | The fluid is a perfect gas.\\ | ||
+ | Heat transfer | ||
+ | Physical properties can be considered constant or dependent of gas mixture and temperature.\\ | ||
+ | The dependence of the heat capacity is considered | ||
+ | </ | ||
+ | === Example of flow with heat transfer === | ||
+ | < | ||
+ | One species only (or homogenous species gas). \\ | ||
+ | The viscosity and the thermal conductivity depend on the Sutherland' | ||
+ | When the buoyancy/ | ||
+ | </ | ||
& | & | ||
+ | | ||
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<note tip> | <note tip> | ||
- | The heat capacity is calculated from the constant of perfect gas ($R=8.3144598 J.mol^{-1}.K^{-1}$) | + | The heat capacity is calculated from the constant of perfect gas ($R=8.3144598 J.mol^{-1}.K^{-1}$), the " |
In the dimensionless form, the specific gas constant is generally equal to unity and the heat capacity is $C_p= \frac{\gamma}{\gamma -1}$. The reference value of the molecular mass must be set to the constant of perfect gas $R$.\\ | In the dimensionless form, the specific gas constant is generally equal to unity and the heat capacity is $C_p= \frac{\gamma}{\gamma -1}$. The reference value of the molecular mass must be set to the constant of perfect gas $R$.\\ | ||
- | If gravity/ | + | If gravity/ |
- | ==== Flows with heat transfer | + | === Multi-species flows === |
+ | < | ||
+ | Heat transfer | ||
+ | Multi-species | ||
+ | Physical | ||
+ | When the buoyancy/ | ||
+ | </ | ||
& | & | ||
+ | | ||
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- | <note important> | + | <note important> |
- | + | In this example, the physical properties are not constant depend on the gas mixture and the temperature. They are calculated in each cell for each time step by means of formulations | |
- | \\ | + | The gas properties |
- | In this example, the physical properties are not constant depend on the gas mixture and the temperature. They are calculated in each cell for each time step by means of formualtions | + | |
- | The gas properties | + |
sunfluidh/fluid_properties_examples.1479460825.txt.gz · Dernière modification : 2016/11/18 10:20 de yann