The Fluid Specific Models tab contains settings for fluid-specific properties. It appears for multiphase simulations and when particles are included in the domain.
Which options are available depends on the simulation set up, including the type and number of fluids used in the simulation (for example, single or multicomponent, single or multiphase, reacting or non-reacting), and whether Additional Variables have been created.
This list box is used to select a fluid (which can, in some cases, represent a solid). The rest of the tab contains settings for the selected fluid.
The Kinetic Theory settings
control the solid particle collision model. When you set Kinetic Theory to Kinetic Theory
, you should set the granular temperature model and radial distribution
function. CFX-Pre will also set the Solid Pressure
Model, Solid Bulk Viscosity, and the Solid Shear Viscosity settings
to Kinetic Theory
.
For details on these settings: |
See: |
---|---|
Granular temperature model | |
Radial distribution function | |
Solid pressure model | |
Solid bulk viscosity | |
Solid shear viscosity |
For modeling information about solid particle collision models, see Solid Particle Collision Models in the CFX-Solver Modeling Guide.
For theoretical information about solid particle collision models, see Solid Particle Collision Models in the CFX-Solver Theory Guide.
If you have set Heat Transfer to Fluid Dependent
on the Fluid Models tab, Heat Transfer Model options appear on
the fluid-specific tabs for each Eulerian phase. If the heat transfer
occurs between two fluids, then additional information must be entered
on the Fluid Pairs tab. Information on heat transfer
between phases is available in Interphase Heat Transfer in the CFX-Solver Modeling Guide.
Some of the available Heat Transfer Model options are similar to those in the single-phase case. See Heat Transfer for details on the following options:
None
Isothermal
Thermal Energy
Total Energy
Additional Heat Transfer Model options include:
Particle Temperature
: Can only be used for particle transport fluids and solids. For details, see Heat Transfer in the CFX-Solver Modeling Guide.Saturation Temperature
: Can only be used for a fluid that is a component of a homogeneous binary mixture. This model is applicable only when the heat transfer modeling is inhomogeneous. For its most common use, one of the phases of a two-phase flow is set to useSaturation Temperature
while the other uses a different Heat Transfer Model option, such asThermal Energy
orTotal Energy
. TheSaturation Temperature
option behaves similarly to theIsothermal
option except that, instead of the fluid temperature being forced to be the specified Fluid Temperature value, the fluid temperature is forced to be the saturation temperature as computed from the saturation properties of the homogeneous binary mixture.Small Droplet Temperature
: Can only be used for a fluid that has Morphology > Option set toDroplets with Phase Change
. For details, see Droplet Condensation Model in the CFX-Solver Modeling Guide.
If you have set Turbulence to Fluid Dependent
on the Fluid Models tab, the Turbulence Model option appears on
the fluid-specific tabs for each Eulerian phase. The models available
are similar to those available in single-phase simulations, with the
following exceptions:
For dispersed fluid, or dispersed/polydispersed solid phases, only the
Dispersed Phase Zero Equation
,Laminar
orZero Equation
models are available. The Dispersed Phase Zero Equation model is the recommended choice. For details, see Phase-Dependent Turbulence Models in the CFX-Solver Modeling Guide.The
LES
andDES
models are available for transient simulations for the continuous phase.
For details, see Turbulence.
The turbulent wall functions are selected automatically, but apply only to the current fluid. For details, see Wall Function.
If you have set the reaction or combustion model to Fluid Dependent on the Fluid Models tab, the Reaction or Combustion Model option can appear on the Fluid Specific Models tab for each Eulerian phase. You will only be able to pick a combustion model for fluids that are reacting mixtures. The models available are similar to those available in single-phase simulations. For details, see:
The erosion properties specified on this form are applied to all wall boundaries. The wall boundaries can also have erosion properties set to override the global settings specified here. For details, see Erosion in the CFX-Solver Modeling Guide.
This option is available for multiphase buoyant flows and/or buoyant flows that include particles (set on the Basic Settings tab). For details, see Buoyancy in Multiphase Flow in the CFX-Solver Modeling Guide.
This is available for Dispersed Solid
Eulerian
phases (phases with Dispersed Solid
as the Morphology setting). For details, see Solid Pressure Force Model in the CFX-Solver Modeling Guide.
This is available for each Eulerian phase in the simulation that is a mixture of more than one component. It does not apply to fluids or solids using the particle tracking model. The options available are the same as those on the Fluid Models tab in a single-phase simulation. For details, see Component Details.
If the component transfer occurs between two fluids, then additional information must be entered on the Fluid Pairs tab. This is only possible when more than one multicomponent fluid exists in a simulation. For details, see Interphase Species Mass Transfer in the CFX-Solver Modeling Guide.
This is available for each Eulerian phase in the simulation
when Additional Variables have been created as well as selected and
set to Fluid Dependent
on the Fluid
Models tab. The options available are the same as those
on the Fluid Models tab in a single-phase simulation.
It does not apply to fluids or solids using the particle tracking
model. For details, see Additional Variable Details.
If the Additional Variable transfer occurs between two fluids, then additional information must be entered on the Fluid Pairs tab. This is possible only when more than one phase in a simulation includes Additional Variables. For details, see Additional Variables in Multiphase Flow in the CFX-Solver Modeling Guide.