VVF18 - Turbulent flow over cylinder
Test case |
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SVTEST196 |
Description
This validation case examines the turbulent flow over a circular cylinder with uniform cross-section. The turbulent flow is simulated for a Reynolds number of 65240, which corresponds to the inlet velocity of 5m/s. This case compares the drag force and drag coefficient results computed by the flow solver with the theoretical results.
Geometry
The geometry consists of an extruded rectangular fluid domain with a cylindrical cavity. The cavity diameter, D, is 0.2 m. The length of the calculation domain in the Z-dir is 1 m. The domain sizes in X and Y directions are 7.5 m and 10 m, respectively.
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This model uses the Advanced Flow solution type.
The swept mesh is made of hexahedral elements. The calculation domain is partitioned into 20 sections.
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The number of elements used in the + Z-dir is 2 without any bias. The following table describes the mesh controls used in the model.
Section | Position | Number of elements | Bias factor | Edge fraction |
---|---|---|---|---|
1 and 3 | X | 18 | start of edge=1.04 | 1 |
Y | 40 | start of edge=1.06 | 1 | |
2 | X | 18 | start of edge=1.04 | 1 |
Y | 100 | no bias | - | |
4 and 5 | X | 100 | no bias | - |
Y | 40 | start of edge=1.06 | 1 | |
6 and 8 | X | 35 | start of edge=1.04 | 1 |
Y | 40 | start of edge=1.06 | 1 | |
7 | X | 35 | start of edge=1.04 | 1 |
Y | 100 | no bias | - | |
9 and 12 | top and bottom sides | 100 | no bias | - |
left and right sides | 35 | start of edge=1.04 | 1 | |
10 and 11 | left and right sides | 100 | no bias | - |
top and bottom sides | 35 | start of edge=1.04 | 1 | |
13 and 16 | top and bottom sides | 100 | no bias | - |
left and right sides | 65 | start of edge=1.0225 | 1 | |
14 and 15 | left and right sides | 100 | no bias | - |
top and bottom sides | 65 | start of edge=1.0225 | 1 | |
17 and 20 | top and bottom sides | 100 | no bias | - |
left and right sides | 60 | start of edge=1.068 | 1 | |
18 and 19 | left and right sides | 100 | no bias | - |
top and bottom sides | 60 | start of edge=1.068 | 1 |
Total number of elements in the model: ~ 163 K
Total number of nodes in the model: ~ 246 K
The fluid is modeled using incompressible air with the following properties:
- Mass density: ρ = 1.207 kg/m3
- Dynamic viscosity: µ = 1.85e-5 Pa·s
- Specific heat at constant pressure: Cp = 1007 J/kg·K
The following boundary conditions are applied:
- Symmetry Plane on the two XY planes.
- Symmetry Plane on the two XZ planes.
- Flow Surface: Boundary Flow Surface on the surface of the cylindrical cavity with No Slip Wall conditions.
- Flow Boundary Condition: Inlet Flow on the topmost wall (+ X-dir) with velocity of 5 m/s with the intensity of 0.01 and eddy length of 0.278 mm (computed from the eddy viscosity ratio of 0.01) set in the Turbulence Characteristics modeling object.
- Flow Boundary Condition: Opening on the bottommost wall (- X-dir) with the same Turbulence Characteristics modeling object as for inlet flow.
- Report Lift and Drag on the cylinder face.
The following solution options are set:
- Turbulence Model: SST - Shear Stress Transport
- Solution Type: Transient
- Transient Setup: Time step = 0.001 s; start time = 0s; end time = 6 s
- Results sampling: at constant time intervals = 0.01 s
- Initial conditions: Uniform with velocity of 0 m/s and the same Turbulence Characteristics modeling object as for inlet flow.
The following solution parameters are set:
- 3D Flow Solver: RMS residual = 1e-5
- 3D Flow Solver: Transient - Iteration Limit = 50
- 3D Flow Solver: Advection scheme for Momentum set to Second-order (SOU)
Theory
Schlichting [55] provides the drag coefficient of circular cylinders as a function of Reynolds number. At the Reynolds number of 65240, the drag coefficient is equal to 1.2. The drag force is computed as follows:
Results
The following figures show the drag force and drag coefficient on the cylinder versus time.
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The following table compares the average drag force and drag coefficient results computed by the flow solver for the last 2 seconds of the simulation with the theoretical results.
Parameters | Theory | Flow solver | Difference,% |
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Drag force, N | 3.621 | 3.530 | 2.51 |
Drag coefficient | 1.2 | 1.17 | 2.5 |