|
[Sponsors] |
Mass balance for eulerian model with thermal phase change |
![]() |
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
![]() |
![]() |
#1 |
Senior Member
Hamed Abdul Majeed
Join Date: May 2012
Location: New Orleans, LA, US
Posts: 147
Rep Power: 14 ![]() |
I have two-phase flow in a domain. There is a phase change in the domain and I have turned on the thermal phase change model. If I monitor the mass flow rates at the inlet and outlet for the mixture they don't match!
Can someone explain this please. I have tried the mass flow rate of the individual phases as well, but the difference is huge! My continuity residuals are of the order 10^-3. Thank you. Regards HM. |
|
![]() |
![]() |
![]() |
![]() |
#2 | |
Senior Member
Join Date: Aug 2014
Location: Germany
Posts: 292
Rep Power: 14 ![]() |
Quote:
|
||
![]() |
![]() |
![]() |
|
|
![]() |
||||
Thread | Thread Starter | Forum | Replies | Last Post |
Condensation with Thermal phase change model | haze_1986 | FLUENT | 0 | August 13, 2017 23:29 |
Wrong flow in ratating domain problem | Sanyo | CFX | 17 | August 15, 2015 06:20 |
Mass Transfer without Phase Change in InterPhaseChangeFoam | Parisa_Khiabani | OpenFOAM Running, Solving & CFD | 5 | May 26, 2015 09:40 |
Thermal Phase Change model | Niru | CFX | 0 | February 21, 2013 13:13 |
error message | cuteapathy | CFX | 14 | March 20, 2012 06:45 |