2-D Transient Flow

Geometry: Transient Plates Ta

Wall Inlet Ta Pa

h

Outlet Pa

Water μ, ρ q

Wall

vb

L • Laminar flow through parallel plates w/ impulsed velocity and heat flux on bottom wall. • Initially at zero velocity and atmospheric temperature.

Parameters Parameter

Symbol

Value

height

h

10 mm

length

L

50 mm

wall velocity

vb

100 mm/s

viscosity

μ

1.831E-5 kg/m-s

density

ρ

1.185 kg/m3

specific heat

c

1004.4 J/kg-K

thermal conductivity

k

0.0261 W/m-K

atmospheric pressure

Pa

1 atm

atmospheric temperature

Ta

298 K

heat flux

q

1000 W/m2

Workbench 1. Create new directory •

called Transient Plates

2. Open ANSYS CFX in this new directory 3. Create New Model •

File – New Simulation



New Simulation window appears.



Select General. Select OK.

4. Save file in new directory: transient_plates.cfx •

File – Save Simulation

5. Import Geometry •

Geometry is same as previously created for Parallel Plates example.



Copy and paste the refined parallel_plates2.gtm into current directory. Rename it transient_plates.gtm.



In Outline View, right-click on Mesh. Select Import Mesh. In Import Mesh window, selected transient_plates.gtm. Click Open.

6. Set Simulation Type •

When CFX opens, in Tree Outline double-click on Simulation Type.



Simulation Type Tab appears.



In Basic Settings Tab under Simulation Type, set Option to Transient.



In Basic Settings Tab under Time Duration, set Total Time to 2 s.



In Basic Settings Tab under Time Steps, set Timesteps to 0.1 s.



Click Apply. Click OK.

7. Define Model Data •

Double-click on Default Domain in Tree Outline. Domain: Default Domain Tab appears.



In General Options Tab under Basic Settings, set Fluids List to Air at 25 C.



In General Options Tab under Domain Models, ensure Reference Pressure is set to 1 atm.



In Fluid Models Tab under Heat Transfer, ensure Option is set to Thermal Energy.



In Fluid Models Tab under Turbulence, set Option to None (Laminar).



Click Apply. Click OK.

8. Define Model Data •

Double-click on Default Domain in Tree Outline. Domain: Default Domain Tab appears.



In Initialisation Tab, select Domain Initialisation. Select Initial Conditions.



Under Cartesian Velocity Components, enter 0 m/s for U, V, and W.



Under Static Pressure, enter 0 Pa for Relative Pressure.



Under Temperature, enter 298 K for Temperature.



Click Apply. Click OK.

9. Check Material Properties •

Outline – Simulation – Materials. Double-click Air at 25 C. Material: Water Tab appears.



In Basic Settings Tab, ensure that Material Group is set to Constant Property Gases.



In Material Properties Tab under Equation of State, ensure that Density is set to 1.185 kg/m3.



In Material Properties Tab under Specific Heat Capacity, ensure that Specific Heat Capacity is set to 1004.4 J/kg-K.



In Material Properties Tab under Transport Properties, ensure that Dynamic Viscosity is set to 1.831E-5 kg/m-s.



In Material Properties Tab under Transport Properties, ensure that Thermal Conductivity is set to 0.0261 W/m-K.



Click Apply. Click OK.

10. Create Inlet Boundary Condition •

Toolbar – Create a Boundary Condition. Enter LetIn for Name. Click OK.



Boundary: LetIn – Basic Settings – Boundary Type. Select Inlet.



Boundary: LetIn – Basic Settings – Location. Select LetIn.



Boundary: LetIn – Boundary Details – Mass and Momentum – Option. Select Static Pressure.



Boundary: LetIn – Boundary Details – Mass and Momentum – Relative Pressure. Enter 0 Pa.



Boundary: LetIn – Boundary Details – Heat Transfer – Static Temperature. Set to 298 K.



Click Apply. Click OK.

11. Create Outlet Boundary Condition •

Toolbar – Create a Boundary Condition. Enter LetOut for Name. Click OK.



Boundary: LetOut – Basic Settings – Boundary Type. Select Outlet.



Boundary: LetOut – Basic Settings – Location. Select LetOut.



Boundary: LetOut – Boundary Details – Mass and Momentum – Option. Select Average Static Pressure.



Boundary: LetOut – Boundary Details – Mass and Momentum – Relative Pressure. Enter 0 Pa.



Click Apply. Click OK.

12. Create Top Wall Boundary Condition •

Toolbar – Create a Boundary Condition. Enter TopWall for Name. Click OK.



Boundary: TopWall – Basic Settings – Boundary Type. Select Wall.



Boundary: TopWall – Basic Settings – Location. Select TopWall.



Boundary: TopWall – Boundary Details – Heat Transfer – Option. Set to Temperature.



Boundary: TopWall – Boundary Details – Heat Transfer – Fixed Temperature. Set to 298 K.



Click Apply. Click OK.

13. Create Bottom Wall Boundary Condition •

Toolbar – Create a Boundary Condition. Enter BottomWall for Name. Click OK.



Boundary: BottomWall – Basic Settings – Boundary Type. Select Wall.



Boundary: BottomWall – Basic Settings – Location. Select BottomWall.



Boundary: BottomWall – Boundary Details. Select checkbox next to Wall Velocity. Enter 0.1 m/s for Wall U, 0 m/s for Wall V, and 0 m/s for Wall W.



Boundary: TopWall – Boundary Details – Heat Transfer. Set to Heat Flux. For Heat Flux in, enter 1000 W/m2.



Click Apply. Click OK.

14. Create First Symmetry Boundary Condition •

Toolbar – Create a Boundary Condition. Enter Sym1 for Name. Click OK.



Boundary: Sym1 – Basic Settings – Boundary Type. Select Symmetry.



Boundary: Sym1 – Basic Settings – Location. Select Sym1.



Click Apply. Click OK.

15. Create Second Symmetry Boundary Condition •

Toolbar – Create a Boundary Condition. Enter Sym2 for Name. Click OK.



Boundary: Sym2 – Basic Settings – Boundary Type. Select Symmetry.



Boundary: Sym2 – Basic Settings – Location. Select Sym2.



Click Apply. Click OK.

File – Save Simulation. transient_plates.cfx.

16. Set Solver Controls •

In Toolbar, select Solver Control

icon.



Solver Control tab appears.



Solver Control – Basic Settings – Timestep Initialisation – Option. Ensure is set to Automatic.



Solver Control – Basic Settings – Convergence Control – Max. Coeff. Loops. Ensure is set to 10.



Solver Control – Basic Settings - Convergence Criteria – Residual Target. Ensure is set to 1.E-4.



Click Apply. Click OK.

17. Set Output Controls •

Note warning message under Viewer. “No intermediate results files...”



In Tree Outline, double-click on Output Control.



Output Control tab appears.



Output Control – Trn Results – Transient Results. Select Add New Item box.



Transient Results window appears. Click OK.



Output Control – Transient Results – Output Frequency. Set Option to Every Timestep.



Click Apply. Click OK.

18. Write Solver File •

In Toolbar, select Write Solver File



Write Solver File window appears.



Save file as transient_plates.def.



Click Save.

icon.

19. Start Run •

Define Run window appears.



Select Start Run.

20. Open CFX-Post •

Once solution is completed, ANSYS CFX Solver Finished Normally window will appear.



Select Yes when asked whether you’d like to post-process results now.

21. Create Plane •

In Toolbar, select Location down menu, select Plane.

icon. In drop-



Insert Plane window appears. Click OK.



Details View – Geometry – Definition – Method. Set to XY Plane.



Details View – Geometry – Definition – Z. Set to 0.0005 m.



Deselect check mark next to Plane 1 in Outline Workspace.

22. Create Vector Plot •

In Toolbar, select Vector

icon.



Insert Vector window appears. Select OK.



In Details View under Geometry tab, for Definition – Locations select Plane 1.



In Details View under Geometry tab, for Definition – Variable ensure that Velocity is selected.



Click Apply.



Right-click in Viewer. Select Predefined Camera – View towards -Z.

23. Alter Legend •

In Outline Workspace under User Locations and Plots, double-click on Default Legend View 1.



In Details View under Definition tab, select Horizontal.



In Details View under Definition tab, for Location – X Justification, select Center.



In Details View under Definition tab, for Location – Y Justification, select Bottom.



In Details View under Appearance tab, for Text Parameters – Precision set 3 and Fixed.



Click Apply.

24. View Other Timesteps •

The default timestep for viewing is the final timestep.



In Toolbar, select Timestep Selector



Timestep Selector window appears.



Select the timestep associated with 0 s. Click Apply.



Repeat for timestep associated with 1 s.

Note that a sub-directory appears in the Transient Plates directory containing a results file for each timestep.

icon.

25. Create Animation •

The default timestep for viewing is the final timestep.



In Toolbar, select Timestep Selector



Timestep Selector window appears.



Select the timestep associated with 0 s. Click Apply.



In Toolbar, select Animation



Animation window appears.



To create first Keyframe, select New icon.



KeyframeNo1 appears in window. Select it and update # of Frames to 21.

icon.

icon.

25. Create Animation (cont.) •

In Timestep Selector window, select timestep associated with 2 s. Click Apply.



In Animation window, select New icon.



Click Play the animation



Select checkbox next to Save MPEG.



Click Play the animation icon again.



Note that a MPG file called cfxMovie.mpg appears in the working directory. This animation may be viewed with Windows Media Player.

icon.

26. Create Contour Plot •

Ensure that 2 s timestep is selected.



In Toolbar, select Contour



Insert Contour window appears. Click OK.



Details View – Geometry – Locations. Set to Plane 1.



Details View – Geometry – Variable. Set to Temperature.



Turn off visibility of vector plot.



Click Apply.

icon.

27. Create Point •

In Toolbar, select Location down menu, select Point.

icon. In drop-



Insert Point window appears. Click OK.



Details View – Geometry – Definition – Method. Ensure it is set to XYZ.



Details View – Geometry – Definition – Point. Set to 0.025 m, 0.005 m, 0 m.



Click Apply.

28. Create Chart •

In Toolbar, select Chart

icon.



Insert Chart window appears. Click OK.



In Details View under Chart tab, ensure that Type is set to Time.



In Details View under Chart Line 1 tab, set Location to Point 1.



In Details View under Chart Line 1 tab, set Time Variable – Variable to Temperature.



Click Apply.



Click Export. Save file to trans_temp.csv.

Transient Temperature Profile 330

Temperature (K)

325 320 315 310 305 300 295 0

0.5

1

1.5

2

Time (s)



Temperature increases as thermal wave passes location.

29. Save State file •

Select File – Save State As, transient_plates.cst.

Analytical Verification •

Penetration depth (δ) of momentum flux from moving wall may be approximated by:

µt δ =4 ρ •

where t is the time since the initial start of the plate.



For time = 0.1 s, the penetration depth is 5.0 mm.

30. Create Line •

In Toolbar, select Location down menu, select Line.

icon. In drop-



Insert Line window appears. Click OK.



Details View – Geometry – Definition – Method. Ensure it is set to Two Points.



Details View – Geometry – Definition – Point 1. Set to 0.05 m, 0 m, 0.0005 m.



Details View – Geometry – Definition – Point 2. Set to 0.05 m, 0.01 m, 0.0005 m.



Details View – Geometry – Line Type – Samples. Set to 20.



Click Apply.

31. Create Chart •

Use Timestep Selector to select results associated with 0.1 s.



In Toolbar, select Chart



Insert Chart window appears. Click OK.



In Details View under Chart tab, ensure that Type is set to XY.



In Details View under Chart Line 1 tab, set Location to Line 1.



In Details View under Chart Line 1 tab, set X Axis – Variable to Velocity u.



In Details View under Chart Line 1 tab, set Y Axis – Variable to Y.



Click Apply.



Click Export. Save file to trans_vel.csv.

icon.

Velocity Profile time = 0.1 s 10

y (mm)

8

6

4

δ ≈ 6.0 mm

2

0 0

20

40

60

80

100

x-velocity (mm/s)



Velocity increases from wall as momentum flux propagates across gap.

Analytical Verification (cont.) •

An analytical expression exists for the x-velocity profile (u) as a function of space (y) and time (t).

u  y ∞  2 = 1 −  − ∑  vb  h  n =1  n π

 2 2 µt   exp  − n π  2 ρ h   

   y    sin  n π       h 



Note for long times, the velocity profiles approaches a linear dependence on y.



Further note, that only the first few terms of the infinite sum actually contribute.

Velocity Profile time = 0.1 s 10

CFX Analytical

y (mm)

8

6

4

2

0 0

20

40

60

80

100

x-velocity (mm/s)



Good agreement between numerical and analytical results.

Practice •

Create an animation of the developing temperature contours.



Does a similar analytical check on the thermal penetration depth yield good agreement?



Why does the plot of transient temperatures at y = 5 mm decrease after the initial increase?



Does the model reach steady-state? How could you predict the time it would take for this geometry to reach steady-state?

Details View - Sites

Domain: Default Domain Tab appears. • In General Options Tab under Basic Settings, set Fluids ... In Fluid Models Tab under Heat Transfer, ensure Option is ... Name. Click OK. • Boundary: LetIn – Basic Settings – Boundary Type. Select. Inlet.

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