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Home / Examples / Fluid Analysis [Bernoulli] / Example 3: Flow around Cylinder

Example 3: Flow around Cylinder


General

  • The steady-state analysis is applied to the flow around the cylinder.
     

  • The flow velocity distribution, the fluid velocity vectors, the streamlines, and the force on the wall face are solved.
     

  • Unless specified in the list below, the default conditions will be applied.
     

  • The above analysis can also be performed by using a circular sheet body as the model and applying [Automatic Fluid Creation].
    The setting for the analysis is described at the end of this explanation.

  • Obtain this session's project file. (Right-click and choose 'Save link as')
    The project has two analysis models.
    ・Analysis Model: Create fluid manually
    ・Analysis Model_Automatic Creation: Create fluid automatically


  • Results will vary depending on Femtet version and the PC environment.

 

Analysis Space

Item

Settings

Analysis Space

2D

Model Unit

mm

 

Analysis Conditions

Item

Tab

Settings

Solver

Solver Selection

Fluid analysis [Bernoulli]

Analysis Type

Fluid Analysis

Steady-state Analysis

Laminar Flow/Turbulent Flow

Fluid Analysis

Select Laminar flow

Flow Type

Fluid Analysis

Select External Flow.

Layer Mesh Setting for Wall Surface (General Settings)

Fluid Analysis

Specify mesh height of 1st layer

Height of 1st Layer Mesh: 0.5 [mm]
Growth Rate: 1.2
Number of Layers: 5

Meshing Setup

Mesh

General mesh size: 10 [mm]

Model

The Air (000_Air) is set to a rectangular sheet body. The boundary conditions of inlet and outlet are set on the left edge and the right edge respectively.

The model is a circle sheet body and the material is iron (007_Fe).

The edges surrounding a circle is a boundary of solid and fluid. Solid wall is automatically set to them.

The outer boundary condition is automatically applied to the top and bottom edges where the boundary condition is not set.

The outer boundary condition will be [Slip Wall] automatically, because [External Flow] specified in the analysis condition comes with one-way forced convection

 

Body Attributes and Materials Setting [Automatic Fluid Creation]

Body Number/Type

Body Attribute Name

Material Name

0/Solid

Air

000_Air(*)

1/Solid

007_Fe *

* Available from the material DB

Boundary Condition

Boundary Condition Name/Topology

Tab

Boundary Condition Type

Setting

Inlet/Edge

Fluid

Inlet

Forced Inflow
Specify flow velocity
0.01 [m/s]

Outlet/Face

Fluid

Outlet

Natural Outflow

 

The outer boundary condition will be [Slip Wall] automatically, because [External Flow] specified in the analysis condition comes with one-way forced convection

 

If the Reynolds number exceeds 100, the time dependency of the turbulence occurs. It makes calculation difficult in the steady-state analysis.

The Reynolds number calculated from this model form, material property, and flow velocity is about 25.2. The steady-state analysis of the laminar flow can be executed.

 

Viscosity μ=1.816e-5 [Pa s]

Density ρ=1.144[kg/m3]

Kinematic viscosity v=μ/ρ=1.816e-5/1.144=1.587e-5 [m2/s]

Flow velocity V=0.01 [m/s]

Diameter of cylinder D=0.04 [m]

Reynolds number Re = V*L/ν=0.01*0.04/1.587e-5 = 25.2

Results

The vectors of the flow velocity distribution around the cylinder are shown below.

The vectors are adjusted to the same length in the graphics setup.

It is known that the so-called twin whirlpools occur behind the cylinder when the Reynolds number is around 30.
Two vortexes appear at the back of the cylinder.

 

 

 

The streamlines are shown below.

The pitch of the startpoints is adjusted in the graphics setup.

The streamlines are generated.

 

 

The force on the wall face is shown by the table.

[Column] shows the force which the cylinder receives from the fluid.

Drag F:The force in the flow direction (X-direction) is 6.58 x 10 ^ -9 [N].

 

 

The coefficient of drag CD can be calculated from the drag F.

 

Thickness in depth direction t = 1 [mm]

Cross sectional area S = D * t = 0.04 * 0.001 = 4e-5 [m2]

Dynamic pressure Pk = 0.5 * ρ*V^2 = 0.5 * 1.144 * 0.01 * 0.01 = 5.720e-5 [Pa]

Coefficient of Drag CD = F / Pk / S = 6.58e-9 / 5.720e-5 /4e-5 = 2.88

 

 

Apply [Automatic Fluid Creation]

For reference, the settings for analysis with [Automatic Fluid Creation] enabled are described below.

Analysis Conditions [Automatic Fluid Creation]

Item

Tab

Settings

Solver

Solver Selection

Fluid analysis [Bernoulli]

Analysis Type

Fluid Analysis

Steady-state Analysis

Laminar Flow/Turbulent Flow

Fluid Analysis

Select Laminar flow

Flow Type

Fluid Analysis

Select External Flow.

Flow Type

Automatic Fluid Creation

Fluid Analysis

Deselect [Set the mesh size of the fluid domain automatically].
Mesh Size of Fluid Domain: 10

External Flow: Forced convection in the +X direction)

External Flow Velocity: 0.01 m/s

Scale Factor for Fluid Domain: 5

Scale Factor for Back Domain of Fluid: 10

Layer Mesh Setting

Fluid Analysis

Specify mesh height of 1st layer

Height of 1st Layer Mesh: 0.5 [mm]
Growth Rate: 1.2
Number of Layers: 5

Meshing Setup

Mesh

General Mesh Size: 2 [mm]

Model [Automatic Fluid Creation]

The model is a circle sheet body and the material is iron (007_Fe).

Body Attributes and Materials Setting [Automatic Fluid Creation]

Body Number/Type

Body Attribute Name

Material Name

1/Solid

007_Fe *

Fluid material 000_Air * is set in the [Automatic Flow Creation] setting.

 

* Available from the material DB

Boundary Conditions [Automatic Fluid Creation]

Set no boundary condition. The external flow direction and velocity are set in the [Automatic Flow Creation] setting.