- •Why CFD is Important for Modeling
- •How the CFD Module Helps Improve Your Modeling
- •Model Builder Options for Physics Feature Node Settings Windows
- •Where Do I Access the Documentation and Model Library?
- •Typographical Conventions
- •Quick Start Guide
- •Modeling Strategy
- •Geometrical Complexities
- •Material Properties
- •Defining the Physics
- •Meshing
- •The Choice of Solver and Solver Settings
- •Coupling to Other Physics Interfaces
- •Adding a Chemical Species Transport Interface
- •Equation
- •Discretization
- •Transport Feature
- •Migration in Electric Field
- •Reactions
- •Reactions
- •Initial Values
- •Initial Values
- •Boundary Conditions for the Transport of Concentrated Species Interface
- •Mass Fraction
- •Mass Fraction
- •Flux
- •Inflow
- •Inflow
- •No Flux
- •Outflow
- •Flux Discontinuity
- •Flux Discontinuity
- •Symmetry
- •Open Boundary
- •Physical Model
- •Transport Properties
- •Model Inputs
- •Fluid Properties
- •Diffusion
- •Migration in Electric Field
- •Diffusion
- •Model Inputs
- •Density
- •Diffusion
- •Porous Matrix Properties
- •Porous Matrix Properties
- •Initial Values
- •Initial Values
- •Domain Features for the Reacting Flow, Concentrated Species Interface
- •Boundary Conditions for the Reacting Flow, Concentrated Species Interface
- •Reacting Boundary
- •Inward Flux
- •Physical Model
- •Transport Properties
- •Fluid Properties
- •Migration in Electric Field
- •Porous Matrix Properties
- •Initial Values
- •Domain Features for the Reacting Flow, Diluted Species Interface
- •Boundary Conditions for the Reacting Flow, Diluted Species Interface
- •Pair and Point Conditions for the Reacting Flow, Diluted Species Interface
- •Multicomponent Mass Transport
- •Multicomponent Diffusion: Mixture-Average Approximation
- •Multispecies Diffusion: Fick’s Law Approximation
- •Multicomponent Thermal Diffusion
- •References for the Transport of Concentrated Species Interface
- •Domain Equations
- •Combined Boundary Conditions
- •Effective Mass Transport Parameters in Porous Media
- •Selecting the Right Interface
- •The Single-Phase Flow Interface Options
- •Laminar Flow
- •Coupling to Other Physics Interfaces
- •The Laminar Flow Interface
- •Discretization
- •The Creeping Flow Interface
- •Discretization
- •Fluid Properties
- •Fluid Properties
- •Mixing Length Limit
- •Volume Force
- •Volume Force
- •Initial Values
- •Initial Values
- •The Turbulent Flow, Spalart-Allmaras Interface
- •The Rotating Machinery, Laminar Flow Interface
- •Rotating Domain
- •Rotating Domain
- •Initial Values
- •Initial Values
- •Rotating Wall
- •Wall
- •Boundary Condition
- •Interior Wall
- •Boundary Condition
- •Inlet
- •Boundary Condition
- •Velocity
- •Pressure, No Viscous Stress
- •Normal Stress
- •Outlet
- •Boundary Condition
- •Pressure
- •Laminar Outflow
- •No Viscous Stress
- •Vacuum Pump
- •Symmetry
- •Open Boundary
- •Boundary Stress
- •Boundary Condition
- •Periodic Flow Condition
- •Flow Continuity
- •Pressure Point Constraint
- •Non-Newtonian Flow—The Power Law and the Carreau Model
- •Theory for the Pressure, No Viscous Stress Boundary Condition
- •Theory for the Laminar Inflow Condition
- •Theory for the Laminar Outflow Condition
- •Theory for the Slip Velocity Wall Boundary Condition
- •Theory for the Vacuum Pump Outlet Condition
- •Theory for the No Viscous Stress Condition
- •Theory for the Mass Flow Inlet Condition
- •Turbulence Modeling
- •Eddy Viscosity
- •Wall Functions
- •Initial Values
- •Wall Distance
- •Inlet Values for the Turbulence Length Scale and Intensity
- •Initial Values
- •The Spalart-Allmaras Turbulence Model
- •Inlet Values for the Turbulence Length Scale and Intensity
- •Pseudo Time Stepping for Turbulent Flow Models
- •References for the Single-Phase Flow, Turbulent Flow Interfaces
- •Selecting the Right Interface
- •Coupling to Other Physics Interfaces
- •Discretization
- •Fluid-Film Properties
- •Initial Values
- •Initial Values
- •Inlet
- •Outlet
- •Wall
- •Symmetry
- •Discretization
- •Initial Values
- •Initial Values
- •Fluid-Film Properties
- •Border
- •Inlet
- •Outlet
- •Conditions for Film Damping
- •The Reynolds Equation
- •Structural Loads
- •Gas Outflow Conditions
- •Rarefaction and Slip Effects
- •Geometry Orientations
- •References for the Thin-Film Flow Interfaces
- •Selecting the Right Interface
- •The Multiphase Flow Interface Options
- •The Relationship Between the Interfaces
- •Bubbly Flow
- •Coupling to Other Physics Interfaces
- •The Laminar Two-Phase Flow, Level Set Interface
- •Discretization
- •The Laminar Two-Phase Flow, Phase Field Interface
- •Domain Level Settings for the Level Set and Phase Field Interfaces
- •Fluid Properties
- •Mixing Length Limit
- •Initial Values
- •Initial Values
- •Volume Force
- •Volume Force
- •Gravity
- •Boundary Conditions for the Level Set and Phase Field Interfaces
- •Wall
- •Boundary Condition
- •Initial Interface
- •The Turbulent Flow, Two-Phase Flow, Level Set Interface
- •The Turbulent Two-Phase Flow, Phase Field Interface
- •Wall Distance Interface and the Distance Equation
- •Level Set and Phase Field Equations
- •Conservative and Non-Conservative Formulations
- •Phase Initialization
- •Numerical Stabilization
- •References for the Level Set and Phase Field Interfaces
- •Stabilization
- •Discretization
- •Level Set Model
- •Initial Values
- •Initial Values
- •Boundary Conditions for the Level Set Function
- •Inlet
- •Initial Interface
- •No Flow
- •Outlet
- •Symmetry
- •Discretization
- •Initial Values
- •Initial Values
- •Phase Field Model
- •Boundary Conditions for the Phase Field Function
- •Initial Interface
- •Inlet
- •Wetted Wall
- •Wetted Wall
- •Outlet
- •The Level Set Method
- •Conservative and Non-Conservative Form
- •Initializing the Level Set Function
- •Variables For Geometric Properties of the Interface
- •Reference for the Level Set Interface
- •About the Phase Field Method
- •The Equations for the Phase Field Method
- •Conservative and Non-Conservative Forms
- •Additional Sources of Free Energy
- •Variables and Expressions
- •Reference For the Phase Field Interface
- •The Laminar Bubbly Flow Interface
- •Reference Pressure
- •Discretization
- •The Turbulent Bubbly Flow Interface
- •Reference Pressure
- •Discretization
- •Fluid Properties
- •Slip Model
- •Initial Values
- •Initial Values
- •Volume Force
- •Volume Force
- •Gravity
- •Gravity
- •Mass Transfer
- •Mass Transfer
- •Boundary Conditions for the Bubbly Flow Interfaces
- •Wall
- •Liquid Boundary Condition
- •Gas Boundary Condition
- •Inlet
- •Liquid Boundary Condition
- •Gas Boundary Condition
- •Outlet
- •Liquid Boundary Condition
- •Gas Boundary Condition
- •Symmetry
- •Gas Boundary Conditions Equations
- •The Mixture Model, Laminar Flow Interface
- •Stabilization
- •Discretization
- •The Mixture Model, Turbulent Flow Interface
- •Stabilization
- •Mixture Properties
- •Mass Transfer
- •Mass Transfer
- •Initial Values
- •Initial Values
- •Volume Force
- •Volume Force
- •Gravity
- •Gravity
- •Boundary Conditions for the Mixture Model Interfaces
- •Wall
- •Mixture Boundary Condition
- •Dispersed Phase Boundary Condition
- •Inlet
- •Mixture Boundary Condition
- •Dispersed Phase Boundary Condition
- •Outlet
- •Mixture Boundary Condition
- •Symmetry
- •The Bubbly Flow Equations
- •Turbulence Modeling in Bubbly Flow Applications
- •References for the Bubbly Flow Interfaces
- •The Mixture Model Equations
- •Dispersed Phase Boundary Conditions Equations
- •Turbulence Modeling in Mixture Models
- •Slip Velocity Models
- •References for the Mixture Model Interfaces
- •Dispersed Phase
- •Discretization
- •Domain Conditions for the Euler-Euler Model, Laminar Flow Interface
- •Phase Properties
- •Solid Viscosity Model
- •Drag Model
- •Solid Pressure Model
- •Initial Values
- •Boundary, Point, and Pair Conditions for the Euler-Euler Model, Laminar Flow Interface
- •Wall
- •Dispersed Phase Boundary Condition
- •Inlet
- •Two-Phase Inlet Type
- •Continuous Phase
- •Dispersed Phase
- •Outlet
- •Mixture Boundary Condition
- •The Euler-Euler Model Equations
- •References for the Euler-Euler Model, Laminar Flow Interface
- •Selecting the Right Interface
- •The Porous Media Flow Interface Options
- •Coupling to Other Physics Interfaces
- •Discretization
- •Fluid and Matrix Properties
- •Mass Source
- •Mass Source
- •Initial Values
- •Initial Values
- •Boundary Conditions for the Darcy’s Law Interface
- •Pressure
- •Pressure
- •Mass Flux
- •Mass Flux
- •Inflow Boundary
- •Inflow Boundary
- •Symmetry
- •No Flow
- •Discretization
- •Fluid and Matrix Properties
- •Volume Force
- •Volume Force
- •Forchheimer Drag
- •Forchheimer Drag
- •Initial Values
- •Initial Values
- •Mass Source
- •Boundary Conditions for the Brinkman Equations Interface
- •Discretization
- •Fluid Properties
- •Porous Matrix Properties
- •Porous Matrix Properties
- •Forchheimer Drag
- •Forchheimer Drag
- •Volume Force
- •Volume Force
- •Initial Values
- •Initial Values
- •Boundary Conditions for the Free and Porous Media Flow Interface
- •Microfluidic Wall Conditions
- •Boundary Condition
- •Discretization
- •Domain, Boundary, and Pair Conditions for the Two-Phase Darcy’s Law Interface
- •Fluid and Matrix Properties
- •Initial Values
- •Initial Values
- •No Flux
- •Pressure and Saturation
- •Pressure and Saturation
- •Mass Flux
- •Inflow Boundary
- •Inflow Boundary
- •Outflow
- •Pressure
- •Darcy’s Law—Equation Formulation
- •About the Brinkman Equations
- •Brinkman Equations Theory
- •References for the Brinkman Equations Interface
- •Reference for the Free and Porous Media Flow Interface
- •Darcy’s Law—Equation Formulation
- •The High Mach Number Flow, Laminar Flow Interface
- •Surface-to-Surface Radiation
- •Discretization
- •Initial Values
- •Initial Values
- •Shared Interface Features
- •Fluid
- •Dynamic Viscosity
- •Inlet
- •Outlet
- •Consistent Inlet and Outlet Conditions
- •Pseudo Time Stepping for High Mach Number Flow Models
- •References for the High Mach Number Flow Interfaces
- •Selecting the Right Interface
- •The Non-Isothermal Flow Interface Options
- •Coupling to Other Physics Interfaces
- •The Non-Isothermal Flow, Laminar Flow Interface
- •Discretization
- •The Conjugate Heat Transfer, Laminar Flow Interface
- •The Turbulent Flow, Spalart-Allmaras Interface
- •Fluid
- •Dynamic Viscosity
- •Wall
- •Boundary Condition
- •Initial Values
- •Pressure Work
- •Viscous Heating
- •Dynamic Viscosity
- •Turbulent Non-Isothermal Flow Theory
- •References for the Non-Isothermal Flow and Conjugate Heat Transfer Interfaces
- •Selecting the Right Interface
- •The Heat Transfer Interface Options
- •Conjugate Heat Transfer, Laminar Flow
- •Conjugate Heat Transfer, Turbulent Flow
- •Coupling to Other Physics Interfaces
- •Accessing the Heat Transfer Interfaces via the Model Wizard
- •Discretization
- •Heat Transfer in Solids
- •Translational Motion
- •Translational Motion
- •Pressure Work
- •Heat Transfer in Fluids
- •Viscous Heating
- •Dynamic Viscosity
- •Heat Source
- •Heat Source
- •Initial Values
- •Initial Values
- •Boundary Conditions for the Heat Transfer Interfaces
- •Temperature
- •Temperature
- •Thermal Insulation
- •Outflow
- •Symmetry
- •Heat Flux
- •Heat Flux
- •Inflow Heat Flux
- •Inflow Heat Flux
- •Open Boundary
- •Periodic Heat Condition
- •Surface-to-Ambient Radiation
- •Boundary Heat Source
- •Boundary Heat Source
- •Heat Continuity
- •Pair Thin Thermally Resistive Layer
- •Pair Thin Thermally Resistive Layer
- •Thin Thermally Resistive Layer
- •Thin Thermally Resistive Layer
- •Line Heat Source
- •Line Heat Source
- •Point Heat Source
- •Convective Cooling
- •Out-of-Plane Convective Cooling
- •Upside Heat Flux
- •Out-of-Plane Radiation
- •Upside Parameters
- •Out-of-Plane Heat Flux
- •Domain Selection
- •Upside Inward Heat Flux
- •Change Thickness
- •Change Thickness
- •Porous Matrix
- •Heat Transfer in Fluids
- •Thermal Dispersion
- •Dispersivities
- •Heat Source
- •Equation Formulation
- •Activating Out-of-Plane Heat Transfer and Thickness
Slip
The Slip condition assumes that there are no viscous effects at both sides of the slip wall and hence, no boundary layer develops. From a modeling point of view, this may be a reasonable approximation if the important effect of the wall is to prevent fluid from leaving the domain.
• Theory for the Slip Wall Boundary Condition in the COMSOL
Multiphysics User’s Guide
See Also
Moving Wall
If the wall moves, so must the fluid on both sides of the wall. Hence, this boundary condition prescribes u = uw. Enter the components of the Velocity of moving wall uw (SI unit: m/s).
Specifying this boundary condition does not automatically cause the associated wall to move. An additional Moving Mesh interface needs to
be added to physically track the wall movement in the spatial reference
Important
frame.
• The Moving Mesh Interface in the COMSOL Multiphysics User’s
Guide
See Also
Inlet
The Inlet node includes a set of boundary conditions describing the fluid flow condition at an inlet. The Velocity boundary condition is the default.
In most cases the inlet boundary conditions appear, some of them slightly modified, in the Outlet type as well. This means that there is nothing in
the mathematical formulations to prevent a fluid from leaving the domain
Tip
through boundaries where the Inlet type is specified.
• Velocity
114 | C H A P T E R 4 : S I N G L E - P H A S E F L O W B R A N C H
•Pressure, No Viscous Stress
•Normal Stress
•Laminar Inflow
•Mass Flow
B O U N D A R Y S E L E C T I O N
From the Selection list, choose the boundaries that represent inlets. See Table 4-4 and
Table 4-5 for available boundary conditions by physics interface.
TABLE 4-4: SINGLE-PHASE FLOW, LAMINAR INLET BOUNDARY CONDITIONS
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TABLE 4-5: SINGLE-PHASE FLOW, TURBULENT INLET BOUNDARY CONDITIONS |
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B O U N D A R Y C O N D I T I O N S F O R T H E S I N G L E - P H A S E F L O W I N T E R F A C E S | 115
V E L O C I T Y
This section displays when Velocity is selected as the Boundary condition. The option is
available for the Inlet and Outlet boundary features.
•Select Normal inflow velocity (the default) to specify a normal inflow velocity magnitude u = nU0 where n is the boundary normal pointing out of the domain. Enter the velocity magnitude U0 (SI unit: m/s).
•If Velocity field is selected, it sets the velocity equal to a given velocity vector u0 when u = u0. Enter the velocity components u0 (SI unit: m/s) to set the velocity equal to a given velocity vector.
Also enter the settings as described in Additional Boundary Condition Settings for Turbulent Flow Interfaces.
P R E S S U R E , N O V I S C O U S S T R E S S
The Pressure, no viscous stress boundary condition specifies vanishing viscous stress along with a Dirichlet condition on the pressure. Enter the Pressure p0 (SI unit: Pa) at the boundary.
This section displays when Pressure, no viscous stress is selected as the Boundary condition. The option is available for the Inlet and Outlet boundary features. Depending on the pressure field in the rest of the
Note domain, an inlet boundary with this condition can become an outlet boundary.
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See Also |
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• Gravity and Boundary Conditions (outlet): Model Library path |
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Also enter the settings as described in Additional Boundary Condition Settings for Turbulent Flow Interfaces.
116 | C H A P T E R 4 : S I N G L E - P H A S E F L O W B R A N C H
N O R M A L S T R E S S
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This section displays when Normal Stress is selected as the Boundary |
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Note |
Boundary Stress features. |
Enter the magnitude of Normal stress f0 (SI unit: N/m2). Implicitly specifies that p f0 .
• Theory for the Normal Stress Inlet Boundary Condition in the
COMSOL Multiphysics User’s Guide
See Also
Also enter the settings as described in Additional Boundary Condition Settings for Turbulent Flow Interfaces.
L A M I N A R I N F L O W
Select a flow quantity to specify for the inlet:
•If Average velocity is selected, enter an Average velocity Uav (SI unit: m/s).
•If Flow rate is selected, enter the Flow rate V0 (SI unit: m3/s).
•If Entrance pressure is selected, enter the Entrance pressure pentr (SI unit: Pa) at the entrance of the fictitious channel outside of the model.
Then specify these parameters:
•Enter the Entrance length Lentr (SI unit: m) to define the length of the inlet channel outside the model domain. This value must be large enough so that the flow can
reach a laminar profile. For a laminar flow, Lentr should be significantly greater than 0.06ReD, where Re is the Reynolds number and D is the inlet length scale (this
formula is exact if D is the diameter of a cylindrical pipe and approximate for other geometries).
B O U N D A R Y C O N D I T I O N S F O R T H E S I N G L E - P H A S E F L O W I N T E R F A C E S | 117
•Select the Constrain endpoints to zero check box to force the laminar profile to go to zero at the bounding points or edges of the inlet channel. Otherwise the velocity is defined by the boundary condition of the adjacent boundary in the model.
For example, if one end of a boundary with a Laminar inflow condition connects to a Slip boundary condition, then the laminar profile has a maximum at that end.
This section displays when Laminar inflow is selected as the Boundary condition for the Laminar Flow interface. However, it is not available
when the Use memory-efficient form check box is selected from Advanced
Note
Settings on the Laminar Flow node’s Settings window.
• Theory for the Laminar Inflow Condition
See Also
A D D I T I O N A L B O U N D A R Y C O N D I T I O N S E T T I N G S F O R T U R B U L E N T F L O W
I N T E R F A C E S
The Turbulent Flow, k- model and Turbulent Flow, low Reynolds number k- models, also requires you to specify k and via one of the following options:
•Select Specify turbulence length scale and intensity to enter values or expressions for the Turbulent intensity IT (unitless) and Turbulence length scale LT (SI unit: m).
The Turbulent intensity IT and Turbulence length scale LT values are related to the turbulence variables via
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•If Specify turbulence variables is selected, enter values or expressions for the Turbulent kinetic energy k0 (SI unit: m2/s2) and Turbulent dissipation rate, 0 (SI unit: m2/s3).
The Turbulent Flow, k- model, also requires you to specify k and via one of the
following option:
•Select Specify turbulence length scale and intensity to enter values or expressions for the Turbulent intensity IT (unitless) and Turbulence length scale LT (SI unit: m).
The Turbulent intensity IT and Turbulence length scale LT values are related to the turbulence variables via
118 | C H A P T E R 4 : S I N G L E - P H A S E F L O W B R A N C H
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•If Specify turbulence variables is selected, enter values or expressions for the Turbulent kinetic energy k0 (SI unit: m2/s2) and Turbulent dissipation rate, 0 (SI unit: 1/s).
For recommendations of physically sound values see Inlet Values for the
Turbulence Length Scale and Intensity.
Tip
For the Turbulent Flow, Spalart-Allmaras interface, also enter a value or expression for the Undamped turbulent kinematic viscosity 0 (SI unit: m2/s).
M A S S F L O W
The mass flow boundary condition is only available for the Inlet boundary type. Depending on the sign of the specified mass flow or flux an inlet boundary with this condition can become an outlet boundary.
Under Mass Flow Rate, select a Mass flow type—Pointwise mass flux, Mass flow rate,
Standard flow rate, or Standard flow rate (SCCM).
• Theory for the Mass Flow Inlet Condition
See Also
Pointwise Mass Flux
This option sets the mass flux parallel to the boundary normal. The flux perpendicular to the normal is set to zero. The mass flux is a model input, which means that COMSOL can take its value from another physics interface if applicable. If User defined is selected from the associated list, the Mass flux Mf (SI unit: kg/(m2·s)) is entered manually in the field. The default value is 0 kg/(m2·s).
Mass Flow Rate
This option sets the integrated mass flow across the entire boundary to a specific value. The mass flow is assumed to be parallel to the boundary normal, so the tangential velocity is set to zero.
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Enter the Normal mass flow rate m (SI unit: kg/s). The default value is 10 5 kg/s.
For 2D models, enter a Channel thickness dbc (SI unit: m). The default value is 1 m.
The Channel thickness is used only in defining the area across which the mass flow occurs—it is not a setting applied to the whole model. Line
2D integrals of mass flux over the boundary in post-processing or coupling variables still produces results per unit thickness and needs to be scaled appropriately for comparison with the specified mass flow.
Standard Flow Rate
This option sets a standard volumetric flow rate, according to the SEMI standard E12-0303. The flow rate is specified as the volumetric flow rate that would occur for the same number of moles per second, if the gas density was a standard value (the molar mass over a fixed standard volume). The flow occurs across the whole boundary in the direction of the boundary normal and is computed by a surface (3D) or line (2D) integral. The tangential flow velocity is set to zero.
The standard density can be defined directly, or by specifying a standard pressure and temperature, in which case the ideal gas law is assumed. Select an option from the
Standard flow rate defined by list—Standard density or Standard pressure and
temperature.
If Standard density is selected enter:
-The Standard flow rate Qsv (SI unit: m3/s) to specify the standard volumetric flow rate through the boundary. The default value is 10 6 m3/s.
-The Standard molar volume Vm (SI unit: m3/mol). The default is 0.0224136 m3/mol.
-The Mean molar mass Mn (SI unit: kg/mol). This can be selected as a model input from another physics interface or set to a user-defined value using the associated
list and field. The default is that User defined is selected from the list with a value of 0.032 kg/mol.
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