|
[Sponsors] |
March 14, 2011, 08:33 |
IDEA viscosity
|
#1 |
New Member
fairus
Join Date: Apr 2010
Posts: 20
Rep Power: 16 |
Dear all,
I tried to plot the Dynamic viscosity of different fuels that are implemented in OpenFOAM using the function given in NSRDSfunc1.H and the coefficients given in liquids/IDEA.C. Based on the plot that I attached, IDEA dynamic viscosity increases after about 550K which is not physical. Does anyone know about this issue? Best Fairus |
|
March 14, 2011, 12:54 |
|
#2 |
Super Moderator
Niklas Nordin
Join Date: Mar 2009
Location: Stockholm, Sweden
Posts: 693
Rep Power: 29 |
Hmmm...I added that. I will look into it tomorrow.
|
|
April 7, 2011, 08:46 |
|
#3 |
Super Moderator
Niklas Nordin
Join Date: Mar 2009
Location: Stockholm, Sweden
Posts: 693
Rep Power: 29 |
Its because the alphaMethyl napthalene properties are the way they are.
I have checked the numbers and they are correct as according to the NSRDS tables. check the viscosity of aC11H10 and you will see how it looks. for more info on how the idea fuel was constructed look into the file src/thermophysicalModels/liquids/IDEA/IDEA.H N |
|
April 7, 2011, 08:50 |
|
#4 |
Super Moderator
Niklas Nordin
Join Date: Mar 2009
Location: Stockholm, Sweden
Posts: 693
Rep Power: 29 |
looking into the table again I see that the valid temperature range for the liquid viscosity is only
250-450 K, which might explain the behavior. |
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Eulerian Modeling: Frictional Viscosity Help | meangreen | FLUENT | 1 | January 25, 2018 16:13 |
Turbulence viscosity limited | Madhukar Rapaka | FLUENT | 0 | June 26, 2006 04:17 |
kinematic viscosity at diff temperatures,pressures | Mecobio | Main CFD Forum | 0 | November 7, 2005 13:55 |
Turbulent viscosity in a riser | ap | FLUENT | 8 | April 19, 2003 09:00 |
Problem of Turbulent Viscosity Ratio Limited | David Yang | FLUENT | 3 | June 3, 2002 07:13 |