CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > Siemens > STAR-CCM+

Pressure drop: Pin-fin heat sink

Register Blogs Community New Posts Updated Threads Search

Like Tree1Likes
  • 1 Post By me3840

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   July 7, 2018, 11:51
Default Pressure drop: Pin-fin heat sink
  #1
New Member
 
Michael Kraus
Join Date: May 2016
Posts: 16
Rep Power: 10
MichaelK is on a distinguished road
Hello everyone,

i have some issues to calculate / simulate the pressure drop over a pin-fin heat sink.

Geometry description:
Heat sink width: 50 mm
Heat sink length: 75 mm
Pin fin diameter: 1 mm
Number of pins in flow direction: 10
Number of pins each row: 10
Pin fin distance (equally distributed) X-direction: 8.22 mm
Pin fin distance (equally distributed) Y-direction: 5.00 mm

To reduce the computation time its converted into a 2D model.
In addition, only one row is simulated (--> "new width = 5 mm")
See Fig. 1 for the Geometry setup

Boundary conditions:
- Velocity inlet: 10 m/s (for example)
- Pressure outlet: 0 Pa
- Two Symetry planes (red walls in Fig.1)

Physics conditions:
- Segregated Flow
- Constant Density
- All y+ Wall Treatment
- Steady
- Two Dimensional
- k-Omega Model
- Turbulent
- Gas

- Ref. Pressure = Initial Pressure = 0 Pa
- Initial Velocity = Inlet Velocity = 10 m/s
- Density and Dynamic Viscosity = constant = default values

Results:
Surface average report at inlet: 82.5 Pa (Fieldfunction: "Pressure")
Fig2 shows the result in a scalar scene.

Problem:
If i compare the CFD result (82.5 Pa) with my analytical result (VDI Heat Atlas - chapter L1.4 (year 2013)) i have a huge gap. See Fig3 and Fig 4

Analytical result:
247.36 Pa





Does anyone know where my mistake is?
Do I forget a setting like reference pressure or pressure coefficient?

Thans a lot!
Attached Images
File Type: jpg Fig1.jpg (39.3 KB, 23 views)
File Type: jpg Fig2.jpg (33.6 KB, 23 views)
File Type: jpg Fig 3.JPG (15.7 KB, 18 views)
File Type: jpg Fig 4.JPG (145.4 KB, 15 views)
MichaelK is offline   Reply With Quote

Old   July 16, 2018, 17:26
Default
  #2
New Member
 
Michael Kraus
Join Date: May 2016
Posts: 16
Rep Power: 10
MichaelK is on a distinguished road
noone ?
MichaelK is offline   Reply With Quote

Old   July 18, 2018, 02:25
Default
  #3
Senior Member
 
Join Date: Nov 2010
Location: USA
Posts: 1,232
Rep Power: 24
me3840 is on a distinguished road
Is 2D really a good assumption here? A pin fin will have significant 3D dynamics that you're ignoring.
MichaelK likes this.
me3840 is offline   Reply With Quote

Old   July 18, 2018, 06:28
Default
  #4
New Member
 
Michael Kraus
Join Date: May 2016
Posts: 16
Rep Power: 10
MichaelK is on a distinguished road
I calculated both, 2D and 3D, versions.
Both Simulations have nearly the same results...

The simulated results are still very different from the analytic ones

What do i wrong?

If you need more information, feel free to ask !
Thanks for your reply!

My fluid is a Gas: Air
MichaelK is offline   Reply With Quote

Old   July 18, 2018, 23:35
Default
  #5
Senior Member
 
Join Date: Nov 2010
Location: USA
Posts: 1,232
Rep Power: 24
me3840 is on a distinguished road
I misread you're using symmetry planes before. Since this is 2D and you're only using a single line of cylinders, is that really comparable to what that book states? It has some sort of grid. Make sure that there isn't anything you're missing since you're doing a 2D analysis to compare to a correlation, which is likely developed from 3D. Are there any area values which you might be misrepresenting? I can't read the text.


I'm not really sure if symmetry planes with only a single cylinder row is a good way to run this. Having multiple cylinders will allow them to shed better if they do indeed do so.
me3840 is offline   Reply With Quote

Reply


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
Simulation of a single bubble with a VOF-method Suzzn CFX 21 January 29, 2018 00:58
Discrepancy between the measurements (pressure drop; VOF) blackemperor FLUENT 2 March 6, 2016 03:40
Mass flow rate prediction of Purge control valve using set pressure drop enr_venkat CFX 11 February 27, 2014 11:30
a problem in calculating pressure drop in Fluent? yu chun FLUENT 1 May 18, 2004 03:40
Hydrostatic pressure in 2-phase flow modeling (long) DS & HB Main CFD Forum 0 January 8, 2000 15:00


All times are GMT -4. The time now is 01:56.