 |
 |
 |
|
|
|
[Sponsors] | ||||
Modelling boundary layer turbulent combustion |
 |
|
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
August 4, 2014, 08:54
|
Modelling boundary layer turbulent combustion
|
#1 |
|
New Member
Rohiit Saini
Join Date: Aug 2014
Posts: 2
Rep Power: 0   |
Hi everyone,
I am trying to model boundary layer turbulent combustion with a global step mechanism i.e C4H6 + 5.5O2 ---> 4CO2 + 3H2O I am following Finite rate/ Eddy Dissipation model but I am confused what to substitute in rate exponent for the above global one step reaction as I don't have molar concentration data with various time intervals. Secondly, as I am using single phase gaseous combustion mechanism, how can I patch the fuel at higher temperature or have to use Multiphase option to patch the fuel near the wall so that I can find Heat transfer to wall as well..?? Kindly help me... Thanx in advance to all.. |
|
|
|
|
|
| Thread Tools | Search this Thread |
| Display Modes | |
|
|
Similar Threads
|
||||
| Thread | Thread Starter | Forum | Replies | Last Post |
| Question about heat transfer coefficient setting for CFX | Anna Tian | CFX | 1 | June 16, 2013 07:28 |
| [snappyHexMesh] Boundary layer in a pipe | Clementhuon | OpenFOAM Meshing & Mesh Conversion | 6 | March 12, 2012 13:41 |
| Set inlet boundary conditions in turbulent boundary layer v2f run | kostas | Main CFD Forum | 0 | March 9, 2012 11:24 |
| Boundary Layer Flow Paradox | Wen Long | Main CFD Forum | 3 | September 24, 2002 09:47 |
| Modelling Transition in the Boundary Layer | Tara | Siemens | 1 | August 15, 2000 09:49 |
Linear Mode
