CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > ANSYS > FLUENT

Using ideal gas law and sutherland law in Fluent

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   July 27, 2009, 15:12
Question Using ideal gas law and sutherland law in Fluent
  #1
New Member
 
Ryan
Join Date: Jul 2009
Location: Windsor
Posts: 9
Rep Power: 17
RyGuy is on a distinguished road
Hello Fluent Users,

I am working on a project regarding the simulation of a process called Low Pressure Cold Spray (also known as Kinetic Spray). I am trying to analyze theoretically the single and multi-phase flow of the process and compare it with experimental data.

Therefore I have created my geometry in Gambit (simple 2d geometry of a convergent-divergent nozzle) and meshed the geometry with quad cells.

I have exported the mesh into Fluent and due to the nature of the process the procedure for setting up the simulation is as follows:

I defined the process using the density based implicit solver, 2D, Steady time enabling the energy equation for thermal considerations. I have selected the k-epsilon standard model and am only considering a single phase supersonic compressible flow. I am using an operating pressure of zero since mach number is greater than 0.1

I have found from literature that it would be ideal to consider the ideal-gas law for the material properties (air) and also the sutherland viscosity law for better accuracy in terms of compressibility and viscous effects.

My main inlet pressure and temperature ranges are 5-10 bars and 500-1000 K, respectively.

When I try to incorporate the ideal gas las for density of air and iterate to get a solution Fluent gives me an Error: floating point error and Error: Object () prompt.

How do I avoid this error? And, if anyone who fully understands Fluent can optimize my procedure for this process can you please provide your input?

Your replies are greatly anticipated....
Thanks in advance!

Ryan
RyGuy is offline   Reply With Quote

Old   July 29, 2009, 20:35
Default
  #2
Senior Member
 
Chris
Join Date: Jul 2009
Location: Ohio, USA
Posts: 169
Rep Power: 17
Chris D is on a distinguished road
Have you tried this? (See 2.1.1)

http://www.cfd-online.com/Wiki/Fluent_FAQ

I had a floating point error today, and reducing the Courant number solved the problem for me.
Chris D is offline   Reply With Quote

Old   July 30, 2009, 11:04
Default
  #3
New Member
 
Ryan
Join Date: Jul 2009
Location: Windsor
Posts: 9
Rep Power: 17
RyGuy is on a distinguished road
Hello Chris,

Sorry I am new to this forum and have not been able to check out the FAQ.
I will give it a try and will keep you posted if it is successful or not.

Thanks for everything,
Ryan
RyGuy is offline   Reply With Quote

Old   June 12, 2012, 15:38
Default
  #4
New Member
 
Tpozkar
Join Date: Jan 2012
Location: Mexico
Posts: 4
Rep Power: 14
Tpozkar is on a distinguished road
Hi RyGuy, I would like if you resolved your problem. I have a similar problem

I´m trying to simulate a compressible flow in a gas turbine, and I get the following error:

Error: Internal error at line 1387 in file '..\..\src\rp_mstage.c'.
Divergence detected in AMG solver

I have tried the suggestions of the fluent_FAQ but I´m not able to resolve my problem.

regards
Tpozkar is offline   Reply With Quote

Old   June 28, 2012, 03:07
Default
  #5
New Member
 
fuxiao
Join Date: Jun 2012
Posts: 2
Rep Power: 0
fuxiao_20 is on a distinguished road
you can try intialize the flow field with a slow speed
fuxiao_20 is offline   Reply With Quote

Reply

Tags
compressible, density, fluent, sutherland


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



All times are GMT -4. The time now is 22:00.