|
[Sponsors] |
Problem with Non-Premixed model (coal burner) |
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
June 4, 2007, 11:44 |
Problem with Non-Premixed model (coal burner)
|
#1 |
Guest
Posts: n/a
|
Hello:
I´m modeling a coal burner with non-premixed model. I´ve got one fuel stream (coal) and two oxidizer stream with different compositions. I must apply two-mixture-fraction approach.(three stream with different composition).DPM iteraction every 25 continuous phase iteraction. I´ve a problem about this approach: Fluent update properties continuous phase every ten iterations. I plot some variables (temperature,O2,mass flow rate). When Fluent do this update properties, these variables increase or decrease its value too much (example: Tempearture changes from 2000 K to 500 K approximately, it changes from 500 to 2000 at the next update it happens every 10 iterations). The solution can´t converge because of these great changes of the fluid properties.I don´t understand this approach. Could somebody explain me two mixture fraction approach? How can i converge my case? My english is so bad.I´m sorry. Thanks |
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Use of k-epsilon and k-omega Models | Jade M | Main CFD Forum | 40 | January 27, 2023 08:18 |
Nonpremixed Combustion Model for Coal Gasification | C.Y.Ler | FLUENT | 2 | April 29, 2014 09:51 |
Polyflow Simulation with ViscoElastic Model memory problem | sid2909 | ANSYS | 0 | May 10, 2010 06:27 |
premixed flame modeling problem | peiyong wang | CFX | 1 | July 18, 2008 13:02 |
A Problem with setting the time step in VOF model | Le | FLUENT | 2 | July 20, 2006 23:00 |