CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > General Forums > Main CFD Forum

different properties different results?!

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   November 17, 2017, 06:19
Default different properties different results?!
  #1
New Member
 
Michele Giovagnoni
Join Date: Sep 2017
Location: Italy
Posts: 12
Rep Power: 9
MikeITA is on a distinguished road
Hi all,

I'm using FLUENT to simulate the solidification process of water. The geometry is a cylinder chilled through the external surface. When I set up the properties of material like a polynomial I obtain perfect results but if I set up the properties of material like a piecewise-linear, for a better accuracy, I obtain not smooth and irregular results. What could be? The boundary conditions are invariated...
Thanks

Mike
MikeITA is offline   Reply With Quote

Old   November 17, 2017, 11:09
Default
  #2
Senior Member
 
Simbelmynė's Avatar
 
Join Date: May 2012
Posts: 551
Rep Power: 16
Simbelmynė is on a distinguished road
Hi,

I guess you mean piecewise polynomial, not piecewise linear?
This depends on the experimental range of validity and should probably be more valid. However, if the transition between different ranges is not smooth then this may be the cause of your non-smooth results. You should check this by a simple hand calculation.

Secondly, why do you wish to change something that gives perfect results?
Simbelmynė is offline   Reply With Quote

Old   November 19, 2017, 00:55
Default
  #3
New Member
 
Michele Giovagnoni
Join Date: Sep 2017
Location: Italy
Posts: 12
Rep Power: 9
MikeITA is on a distinguished road
Hi Symbelmyne,

no sorry, I wrote well. I know piecewise-polynomial would be better but in my case some water properties have a gap at the transition temperature so a piecewise-linear gives to me a good accuracy as well. First I want change the properties even if I have smooth results because a polynomial function don't fit very well the real trend of the properties. Second that results are smooth but different from my experimental results.

Anyway you probably are right, that irregular results are caused by the gap that, for instance, the thermal conductivity has at the transition temperature. Is there something I could do to regularize the results?

Thanks very much for your help.

Mike
MikeITA is offline   Reply With Quote

Old   November 19, 2017, 14:48
Default
  #4
Senior Member
 
Simbelmynė's Avatar
 
Join Date: May 2012
Posts: 551
Rep Power: 16
Simbelmynė is on a distinguished road
I am not sure what you mean by regularize the results.

Have you compared the results to experimental data?

and in that case

Is there a large discrepancy compared to experimental data?

Your solidification front might need a very fine mesh to resolve it properly. Have you done a mesh sensitivity study to rule out possible effects of the mesh size?
Simbelmynė is offline   Reply With Quote

Old   November 19, 2017, 23:12
Default
  #5
New Member
 
Michele Giovagnoni
Join Date: Sep 2017
Location: Italy
Posts: 12
Rep Power: 9
MikeITA is on a distinguished road
During the transition the temperature should be constant but I obtain an oscillation, so with regularize I mean see clear results and linear during the phase changed. I compared the results with the experimental data and they have a large discrepancy, the temperature during the solid-liquid transition can swing around from -2 to +2 degrees when should be a constant value (0 degrees).

The mesh is very fine and it's ok, considering that I have a 2D geometry and I'm doing a axisimmetric simulation. I've done a mesh analysis and all the parameters are ok.
MikeITA is offline   Reply With Quote

Old   November 20, 2017, 13:25
Default
  #6
Senior Member
 
Simbelmynė's Avatar
 
Join Date: May 2012
Posts: 551
Rep Power: 16
Simbelmynė is on a distinguished road
Not sure what it can be in this case. You have a very low latent heat I guess if there is no temperature change during the phase transition. Are the experimental measurements published, and if so do you have a reference?

Anyways, with the polynomial expression your simulation fits the experimental data perfectly? In this case the gaps in the piecewise expression seems to be the problem (although I do not understand why you wish to use a piecewise expression when the polynomial expression fits the experiments perfectly).
Simbelmynė is offline   Reply With Quote

Old   November 20, 2017, 22:23
Default
  #7
New Member
 
Michele Giovagnoni
Join Date: Sep 2017
Location: Italy
Posts: 12
Rep Power: 9
MikeITA is on a distinguished road
firstly thanks for all the time you are dedicating to me. Secondly the experimental data are obtained by the experiments I'm doing.

With the polynomial expression the results are smooth and clear but not like the experimental data. I wish to use a piecewise expression because a unique polynomial can't fit perfectly the property trend. The thermal conductivity, like density or specific heat of water, has a big gap in corrispondence of 0 degrees.

Here my email, contact me if you are interested to receive some pictures. I can't upload them on the website:
n1705195j@e.ntu.edu.sg

Thanks again

Mike
MikeITA is offline   Reply With Quote

Reply

Tags
heat fluxes, properties of fluid, result change


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
Save Results automatically by APDL Command ansyxyz ANSYS 1 June 5, 2018 09:16
OpenFOAM - Validation of Results Ahmed OpenFOAM Running, Solving & CFD 10 May 13, 2018 19:28
Transient Run - Output "Time" in partial results? evcelica CFX 2 May 16, 2012 22:36
error message cuteapathy CFX 14 March 20, 2012 07:45
Properties of air versus temperature AND pressure Vincent Main CFD Forum 5 July 28, 2008 07:28


All times are GMT -4. The time now is 12:19.