|
[Sponsors] |
OF 2.3.1 PengRobinsonGas only with Sutherland transport? |
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
February 26, 2015, 10:02 |
OF 2.3.1 PengRobinsonGas only with Sutherland transport?
|
#1 |
New Member
Eugen
Join Date: Sep 2014
Posts: 18
Rep Power: 11 |
I was about to use the PengRobinson Equation of State and recognised that users are only allowed to use it with temperature dependent transport properties, as sutherland or polynomial transport.
Why does this restriction exist? Logical reasons such like: if the user needs real gas equation of state he would have high temperatures and therefore rather should use temperature depedent transport than constant transport properties or are there other reasons? |
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Using PengRobinsonGas EoS with sprayFoam | Jabo | OpenFOAM Running, Solving & CFD | 35 | April 29, 2022 15:35 |
[blockMesh] blockMesh (of 2.3.1) fails for wedge | josefrito | OpenFOAM Meshing & Mesh Conversion | 0 | February 8, 2015 08:10 |
OpenFOAM Foundation releases OpenFOAMŪ 2.3.1 | CFDFoundation | OpenFOAM Announcements from OpenFOAM Foundation | 4 | February 8, 2015 05:19 |
[OpenFOAM.org] Problem of openFOAM 2.3.1 installation in Ubuntu 14.04LTS | mukut | OpenFOAM Installation | 9 | January 19, 2015 00:48 |
PengRobinsonGas crashing with high pressures on fine mesh | Jabo | OpenFOAM Running, Solving & CFD | 6 | January 13, 2015 10:43 |