|
[Sponsors] |
Which method is better to post-process for mass and energy flows? |
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
December 12, 2011, 16:21 |
Which method is better to post-process for mass and energy flows?
|
#1 |
Senior Member
Join Date: Oct 2010
Location: Zurich
Posts: 176
Rep Power: 16 |
If one wants to calculate mass and energy flows at various planes in a domain, which one of the following methods is more accurate?
1. Calculate these inside CFX-Post using functions like massFlowInt, massflowave etc. on variables like velocity u, velocity v, velocity w, area, static enthalpy etc. 2. Export these values on the required planes to text files and then use these text files to calculate the relevant quantities through say MATLAB. Thanks for your inputs |
|
December 12, 2011, 18:13 |
|
#2 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,854
Rep Power: 144 |
Option 1 is most accurate. This will use the integration points used by the solver so will maintain the solver accuracy. Option 2 only uses the nodal values and so will introduce a difference to approach used int he solver.
|
|
December 13, 2011, 06:21 |
|
#3 |
Senior Member
Join Date: Oct 2010
Location: Zurich
Posts: 176
Rep Power: 16 |
Thanks Glen for your reply.
I agree completely. However, in one of my simulations, I had to calculate the heat transfer coefficient (HTC) for heat transfer from wall to fluid in channel flow at various axial locations along the channel. I defined HTC at any axial location x as per the traditional definition as Average heat flux at x = HTC (x)*(Average Twall(x) - Tbulk(x)) Since Average heat flux at x, Average Twall(x) at any axial location x and Tbulk(x) at the corresponding axial location were not available from CFX-Post, I had to export the nodal heat flux, Twall and Tfluid values along several axial planes and then use this info available in exported text files to calculate HTC(x) in MATLAB. I understand that using nodal values would not have given me accurate values of HTC(x), but could I have done anything better? |
|
December 13, 2011, 17:08 |
|
#4 | |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,854
Rep Power: 144 |
Quote:
This could also be done with a script in CFD-Post which takes strips of your geometry and does integrations on the strip. It would have required a little programming of session files to work I suspect. |
||
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Mass and energy source - evaporation | neilduffy1024 | ANSYS | 4 | July 17, 2013 00:50 |
total energy and mass balances | megacrout | OpenFOAM | 3 | October 20, 2011 10:09 |
ATTENTION! Reliability problems in CFX 5.7 | Joseph | CFX | 14 | April 20, 2010 16:45 |
Mass and Energy residue | gxue | Main CFD Forum | 0 | October 14, 2009 15:57 |
Mass transfer Term in Mixture Energy Equation | CFDtoy | Main CFD Forum | 0 | July 3, 2008 17:14 |