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© Fluent Inc. 06/06/22 C1 Fluent Software Training TRN-98-006 Boundary Conditions
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Page 1: Fluent.4.Boundary

© Fluent Inc. 04/07/23C1

Fluent Software TrainingTRN-98-006

Boundary Conditions

Page 2: Fluent.4.Boundary

© Fluent Inc. 04/07/23C2

Fluent Software TrainingTRN-98-006

Outline

Purpose of Boundary Conditions Setting Boundary Conditions

Flow Inlets and Exits Wall, Repeating, and Pole Boundaries Internal Cell Zones Internal Face Boundaries

Page 3: Fluent.4.Boundary

© Fluent Inc. 04/07/23C3

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Purpose of Boundary Conditions Boundary Conditions

Boundaries direct and constrain motion of flow. Boundary Conditions are a required component of mathematical model.

Specify fluxes into computational domain of: Mass Momentum Energy

Boundary Conditions are assigned to Zones. Zones are a collection of cells (fluid or solid continuum)

or cell faces (boundaries, interior surfaces). Surfaces are used for post-processing. Surfaces can correspond to Zones:

Surfaces are automatically generated from cell face Zones. Surfaces corresponding to fluid and solid zones are not.

K.E. of turbulence Dissipation rate of turbulence Species mass fractions

out

walls

in

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Setting Boundary Conditions To set boundary conditions for particular zone:

Define Boundary Conditions... Choose the zone in Zone list. Click on selected zone type in Type list Click Set.. button

Can also select boundary zone in graphics window using right mouse button.

Useful if: Setting up problem for first time Two or more zones of same type in problem.

Page 5: Fluent.4.Boundary

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Flow Inlets and Exits - Introduction Wide range of boundary conditions permit flow to enter and exit

solution domain. Types of boundary conditions for specification of flow inlets and

exits: General

Pressure inlet Pressure outlet

Incompressible Velocity inlet Outflow

Compressible flows Mass flow inlet Pressure far-field

Special Inlet vent, outlet vent, intake fan, exhaust fan

Page 6: Fluent.4.Boundary

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Inlet and Outlet Boundaries

Inlet and Outlet boundary conditions are available to specify fluxes for: Internal Flows: jet engine, reactor External Flows: aircraft in flight, natural convection flows

General guidelines: Select inlet and outlet boundary location and shape such that flow either

goes in or out. Not necessary, but will typically observe better convergence.

Should not observe large gradients in direction normal to boundary. Indicates incorrect set-up.

Minimize grid skewness near boundary.

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Velocity Inlets (1)

Defines velocity and scalar properties of flow at inlet boundaries.

Useful when velocity or velocity profile is known at inlet.

Intended for incompressible flows only.

Total (or stagnation) properties of flow are not fixed.

Stagnation properties vary to accommodate prescribed velocity distribution.

Use in compressible flows non-physical result

Page 8: Fluent.4.Boundary

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Velocity Inlets (2)

User-defined functions (UDF) can be used to define spatial- and time- varying velocity profiles (magnitude and direction).

If upstream flow comes from region of constant total energy and there are no losses (upstream), it may be easier to use the Pressure Inlet condition.

Still need to specify direction of velocity vector. Don’t place velocity inlet too close to a solid obstruction.

Can force the solution to be non-physical, e.g., imposes velocity field, etc., at boundary that may not be intended.

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Determining Turbulence Parameters When turbulent flow enters domain at inlet, outlet, or at a far-field

boundary, FLUENT 5 requires boundary values for: Turbulent kinetic energy k

Four methods available for specifying turbulence parameters: Set k and explicitly Set turbulence intensity and turbulence length scale Set turbulence intensity and turbulent viscosity ratio Set turbulence intensity and hydraulic diameter

Intensity and length scale depend on conditions upstream, e.g.: Exhaust of a turbine

Intensity = 20 % Length scale = 1 - 10 % of blade span Downstream of perforated plate or screen

Intensity = 10 % Length scale = screen/hole size Fully-developed flow in a duct or pipe

Intensity = 5 % Length scale = hydraulic diameter

Turbulence dissipation rate

Page 10: Fluent.4.Boundary

© Fluent Inc. 04/07/23C10

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Pressure Preliminaries

Absolute pressure is referenced to a vacuum.

Can be expressed relative to operating pressure as the gauge pressure:

Static pressure is thermodynamic pressure (Stoke’s Hypothesis).

Expressible as absolute or gauge pressure

Boundary conditions require gauge pressure inputs.

operatinggaugeabsolute ppp

gauge pressure

operating pressure

pressure level

operating pressure

absolute pressure

vacuum

Page 11: Fluent.4.Boundary

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Calculations Using Pressure

Total (stagnation) pressure is defined as:

Pressure at thermodynamic state which would exist if fluid were brought to rest (zero velocity) isentropically.

1/2 v2 is referred to as the dynamic pressure. Density can be calculated from the ideal gas law:

For incompressible flow:

For compressible flow:

ptotal = pstatic + 1/2 v2

p

RTabsolute

p

RToperating

Page 12: Fluent.4.Boundary

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Setting Operating Pressure

For compressible flows: Set operating pressure = 0 Treat gauge pressures as absolute pressures

For incompressible, constant-density flows, operating pressure not used.

For incompressible flows using ideal-gas law to determine density Select incompressible-ideal-gas in Define Materials... Set operating pressure close to mean pressure in problem.

Page 13: Fluent.4.Boundary

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Pressure Inlet Boundary (1) Defines total pressure, temperature, and

other scalar quantities at flow inlets. Also requires direction of velocity

vector to be defined. Can get non-physical results if you

don’t specify reasonable direction for velocity vector.

Useful when: flow rate and/or velocity is not known

(e.g., buoyancy-driven flows). “free” boundary in an external or

unconfined flow needs to be defined. Suitable for compressible and

incompressible flows.

Page 14: Fluent.4.Boundary

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Pressure Inlet Boundary (2)

Inflow stagnation properties are prescribed: Mechanical head of pressure/total pressure drives flow into

computational domain. Mass flux varies depending on interior solution and direction specified

for velocity vector. Note:

Value specified for total pressure used as static pressure wherever outflow occurs.

Total temperature set to static temperature for incompressible flows.

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Pressure Outlet Boundary (1) Flow exits computational domain at

fixed static pressure. Requires specification of static

(gauge) pressure at outlet boundary. All other flow quantities at the

pressure outlet boundary are extrapolated from the interior.

Value of specified static pressure: used only while exit flow is

subsonic. ignored for supersonic flow

(pressure is extrapolated from flow in interior).

Page 16: Fluent.4.Boundary

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Pressure Outlet Boundary (2)

“Backflow” conditions must be specified. Required for calculations if flow reverses direction at Pressure Outlet boundary

during solution process. When backflow occurs, it is assumed to be normal to the boundary.

Cannot specify the direction of the flow entering the domain, in contrast to pressure inlet boundary condition.

Convergence difficulties minimized by realistic values for backflow quantities. Value specified for static pressure used as total pressure wherever backflow

occurs. Pressure Outlet must be used when problem is set up with Pressure Inlet.

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Outflow Boundary

Flow exiting domain at Outflow boundary has zero normal gradients for all flow variables except pressure.

FLUENT extrapolates required information from interior. Useful when:

Details of flow velocity and pressure not known prior to solution of flow problem.

Appropriate where exit flow is close to fully developed condition. Note: Use of Pressure Outlet (instead of Outflow) often results in

better rate of convergence when backflow occurs during iteration.

Page 18: Fluent.4.Boundary

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outflow condition ill-posed

outflow condition not obeyed

outflow condition obeyed

outflow condition closely obeyed

Restrictions on Outflow Boundaries Outflow Boundaries cannot be used:

with compressible flows. with the Pressure Inlet boundary condition (use Velocity Inlet instead):

Combination does not uniquely set a pressure gradient over the whole domain. in unsteady flows with variable density.

Do not use outflow boundaries where:

Flow enters domain Gradients in flow

direction are significant Conditions downstream

of exit plane impact flow in domain

Page 19: Fluent.4.Boundary

© Fluent Inc. 04/07/23C19

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Modeling Multiple Exits Using Outflow boundary condition:

Mass flow divided equally among all outflow boundaries by default.

Flow Rate Weighting (FRW) set to 1 by default.

For uneven flow distribution: specify Flow Rate Weighting for each

outflow boundary: mi=FRWi/FRWi. static pressure varies among exits to

accommodate flow distribution.

Can also use Pressure Outlet boundariesto define exits.

pressure-inlet (p0,T0) pressure-outlet (ps)2

velocity-inlet (v,T0)pressure-outlet (ps)1

or

FRW2

velocity inlet

FRW1

Page 20: Fluent.4.Boundary

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Other Inlet/Outlet Boundary Conditions Mass Flow Inlet

Used in compressible flows to prescribe mass flow rate at inlet. Not required for incompressible flows.

Pressure Far Field Available when density is calculated from the ideal gas law. Used to model free-stream compressible flow at infinity, with free-stream

Mach number and static conditions specified. Exhaust Fan/Outlet Vent

Model external exhaust fan/outlet vent with specified pressure jump/loss coefficient and ambient (discharge) pressure and temperature.

Inlet Vent/Intake Fan Model inlet vent/external intake fan with specified loss coefficient/

pressure jump, flow direction, and ambient (inlet) pressure and temperature.

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Wall, Repeating, and Pole Boundaries

Purpose of Boundary Conditions Setting Boundary Conditions

Flow Inlets and Exits Wall, Repeating, and Pole Boundaries

Wall Symmetry Periodic Axis

Internal Cell Zones Internal Face Boundaries

Page 22: Fluent.4.Boundary

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Wall Boundaries Used to bound fluid and solid regions. In viscous flows, no-slip condition

enforced at walls Tangential velocity component

specified in terms of translational or rotational motion of wall boundary.

Wall shear stress and heat transfer based on local flow field.

Assumed to be rigid and impermeable Normal velocity component = 0

For accurate predictions of wall shear stress, be sure to resolve boundary layers in viscous flows.

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Symmetry Boundaries

Used to reduce computational effort in problem. Flow field and geometry must be symmetric:

Zero normal velocity at symmetry plane Zero normal gradients of all variables at symmetry plane

No inputs required. Must take care to correctly define symmetry boundary locations.

Also used to model slip walls in viscous flow

symmetry planes

Page 24: Fluent.4.Boundary

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Periodic Boundaries Used when physical geometry of

interest and expected pattern of flow/thermal solution have periodically repeating nature.

Reduces computational effort in problem.

Two types available in FLUENT 5. Type 1: Does not allow pressure

drop across periodic planes. Type 2: Periodic boundaries with

pressure drop.

4 tangential inlets

cyclic boundaries

IJ

Periodic at I=NI

Periodic at I=1

Rotationally periodic

Translationally periodic

Page 25: Fluent.4.Boundary

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Periodic Boundaries with Pressure Drop - Type 2

MUST be translationally periodic Designed to model fully-developed conditions

Fully-developed flow in pipes and ducts Tube banks

Periodic heat transfer also possible Specify either:

Mean pressure gradient per period

Net mass flow rate

computational domain

Streamlines in a 2D tube heat exchanger

flow direction

Page 26: Fluent.4.Boundary

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Axis Boundaries

Used: At centerline (y=0) of an

axisymmetric grid Where multiple grid lines meet

at a point in a 3D O-type grid Specify:

No inputs required

AXIS boundary

Page 27: Fluent.4.Boundary

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Fluent Software TrainingTRN-98-006

Internal Cell Zones

Purpose of Boundary Conditions Setting Boundary Conditions

Flow Inlets and Exits Wall, Repeating, and Pole Boundaries Internal Cell Zones

Fluid Porous

Type of fluid zone Solid

Internal Face Boundaries

Page 28: Fluent.4.Boundary

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Fluid Conditions Fluid zone = group of cells for which all

active equations are solved. Only required input is type of fluid

material So appropriate material properties

used Optional inputs allow setting of

source terms: Heat Mass Momentum

Can define motion for fluid zone If rotationally periodic boundaries adjacent to fluid zone, use rotation axis. Define fluid zone as laminar flow region if modeling transitional flow.

Turbulence Species

Page 29: Fluent.4.Boundary

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Porous Media Conditions Porous zone modeled as special type of fluid zone.

Enable Porous Zone option in Fluid panel. Pressure loss in flow determined via user inputs.

Used to model flow through porous media and other “distributed” resistances:

Packed beds Filter papers Perforated plates Flow distributors Tube banks

Page 30: Fluent.4.Boundary

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Solid Conditions “Solid” zone = group of cells for which only

heat conduction problem solved. No flow equations solved

Material being treated as solid may actually be fluid, but it is assumed that no convection takes place.

Only required input is material type So appropriate material properties used.

Optional inputs allow you to set volumetric heat generation rate (heat source).

Can define motion for solid zone Need to specify rotation axis if rotationally

periodic boundaries adjacent to solid zone.

Page 31: Fluent.4.Boundary

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Internal Face Boundaries

Defined on cell faces Do not have finite thickness Provide means of introducing step change in flow properties.

Used to implement physical models representing: Fans Radiators Porous jump

Thin porous membranes Interior wall

Page 32: Fluent.4.Boundary

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Fluent Software TrainingTRN-98-006

Summary

Zones are used to assign boundary conditions. Wide range of boundary conditions permit flow to enter and exit

solution domain. Wall boundary conditions used to bound fluid and solid regions. Repeating boundaries used to reduce computational effort. Internal cell zones used to specify fluid, solid, and porous regions. Internal face boundaries provide way to introduce step change in flow

properties.