CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > OpenFOAM

reactingFoam: adiabatic flame temperature

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   July 29, 2009, 06:22
Default reactingFoam: adiabatic flame temperature
  #1
New Member
 
Frederick
Join Date: Jul 2009
Posts: 3
Rep Power: 16
rFkhemek is on a distinguished road
Hello,

I am using reactingFoam for simulation of premixed laminar flames. I noticed that the maximum flame temperature continues to increase much beyond adiabatic flame temperature.

Does anyone have idea why this is happening?

Frederick
rFkhemek is offline   Reply With Quote

Old   July 31, 2009, 04:11
Default
  #2
Member
 
Christof Benz
Join Date: Mar 2009
Posts: 52
Rep Power: 17
chbenz is on a distinguished road
Hi,

could you tell us a bit more of your case setting?

Christof
chbenz is offline   Reply With Quote

Old   July 31, 2009, 06:42
Default rxn mech.
  #3
New Member
 
Frederick
Join Date: Jul 2009
Posts: 3
Rep Power: 16
rFkhemek is on a distinguished road
Christof,

I just noticed that this problem of flame temperature (FT) peeking to 4000 K & above is something not specific only to the case with new reaction mechanism. I ran the reactingFoam tutorial case for heptane, and without exception FT is again increasing uncontrollably.

Pasted below is the output for a few i.steps:

Solving chemistry
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
DILUPBiCG: Solving for Ux, Initial residual = 0.000106553, Final residual = 3.70098e-08, No Iterations 1
DILUPBiCG: Solving for Uy, Initial residual = 0.000307872, Final residual = 1.29959e-07, No Iterations 1
DILUPBiCG: Solving for C7H16, Initial residual = 0.000136574, Final residual = 3.75731e-08, No Iterations 1
DILUPBiCG: Solving for O2, Initial residual = 1.15028e-05, Final residual = 4.19287e-08, No Iterations 1
DILUPBiCG: Solving for CO2, Initial residual = 5.6045e-05, Final residual = 3.30845e-08, No Iterations 1
DILUPBiCG: Solving for H2O, Initial residual = 5.6045e-05, Final residual = 3.30845e-08, No Iterations 1
DILUPBiCG: Solving for h, Initial residual = 0.000146672, Final residual = 4.47212e-08, No Iterations 1
DICPCG: Solving for p, Initial residual = 0.0098115, Final residual = 8.23315e-10, No Iterations 94
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
time step continuity errors : sum local = 1.37979e-13, global = 5.5059e-16, cumulative = 4.67128e-13
DICPCG: Solving for p, Initial residual = 0.000684229, Final residual = 9.72282e-10, No Iterations 80
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
time step continuity errors : sum local = 1.28656e-13, global = -1.25894e-15, cumulative = 4.65869e-13
DILUPBiCG: Solving for epsilon, Initial residual = 2.20208e-05, Final residual = 3.70251e-09, No Iterations 1
DILUPBiCG: Solving for k, Initial residual = 8.20206e-05, Final residual = 2.26324e-08, No Iterations 1
ExecutionTime = 3027.24 s ClockTime = 3034 s

Max Temperature = 5004.46 K

Density = 1.50653 kg/m3

h Value = 537143 J/kg/K

Courant Number mean: 0.0145809 max: 0.0987632
deltaT = 2.43902e-05
Time = 0.0831951

Solving chemistry
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
DILUPBiCG: Solving for Ux, Initial residual = 0.000116581, Final residual = 3.36492e-08, No Iterations 1
DILUPBiCG: Solving for Uy, Initial residual = 0.000437282, Final residual = 1.29249e-07, No Iterations 1
DILUPBiCG: Solving for C7H16, Initial residual = 0.000136563, Final residual = 3.7544e-08, No Iterations 1
DILUPBiCG: Solving for O2, Initial residual = 1.14962e-05, Final residual = 3.73572e-08, No Iterations 1
DILUPBiCG: Solving for CO2, Initial residual = 5.60065e-05, Final residual = 3.38653e-08, No Iterations 1
DILUPBiCG: Solving for H2O, Initial residual = 5.60065e-05, Final residual = 3.38653e-08, No Iterations 1
DILUPBiCG: Solving for h, Initial residual = 0.000146659, Final residual = 4.46909e-08, No Iterations 1
DICPCG: Solving for p, Initial residual = 0.021823, Final residual = 7.99519e-10, No Iterations 94
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
time step continuity errors : sum local = 1.39516e-13, global = 6.78508e-16, cumulative = 4.66548e-13
DICPCG: Solving for p, Initial residual = 0.0010358, Final residual = 8.53631e-10, No Iterations 78
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
time step continuity errors : sum local = 1.2852e-13, global = -3.65466e-16, cumulative = 4.66182e-13
DILUPBiCG: Solving for epsilon, Initial residual = 2.1987e-05, Final residual = 3.94527e-09, No Iterations 1
DILUPBiCG: Solving for k, Initial residual = 8.18932e-05, Final residual = 2.20388e-08, No Iterations 1
ExecutionTime = 3028.26 s ClockTime = 3035 s

Max Temperature = 5004.55 K

Density = 1.50653 kg/m3

h Value = 537143 J/kg/K

Courant Number mean: 0.0145802 max: 0.0987639
deltaT = 2.43902e-05
Time = 0.0832195

Solving chemistry
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
DILUPBiCG: Solving for Ux, Initial residual = 0.000114486, Final residual = 3.12228e-08, No Iterations 1
DILUPBiCG: Solving for Uy, Initial residual = 0.000386029, Final residual = 1.17461e-07, No Iterations 1
DILUPBiCG: Solving for C7H16, Initial residual = 0.000136565, Final residual = 3.75133e-08, No Iterations 1
DILUPBiCG: Solving for O2, Initial residual = 1.14759e-05, Final residual = 3.74779e-08, No Iterations 1
DILUPBiCG: Solving for CO2, Initial residual = 5.60046e-05, Final residual = 3.35481e-08, No Iterations 1
DILUPBiCG: Solving for H2O, Initial residual = 5.60046e-05, Final residual = 3.35481e-08, No Iterations 1
DILUPBiCG: Solving for h, Initial residual = 0.000146682, Final residual = 4.46701e-08, No Iterations 1
DICPCG: Solving for p, Initial residual = 0.0181925, Final residual = 9.03279e-10, No Iterations 90
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
time step continuity errors : sum local = 1.36605e-13, global = 1.02321e-15, cumulative = 4.67205e-13
DICPCG: Solving for p, Initial residual = 0.000779756, Final residual = 9.12506e-10, No Iterations 75
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
time step continuity errors : sum local = 1.26039e-13, global = 3.33582e-16, cumulative = 4.67539e-13
DILUPBiCG: Solving for epsilon, Initial residual = 2.19667e-05, Final residual = 3.60779e-09, No Iterations 1
DILUPBiCG: Solving for k, Initial residual = 8.18277e-05, Final residual = 2.25868e-08, No Iterations 1
ExecutionTime = 3029.38 s ClockTime = 3036 s

Max Temperature = 5004.64 K

Density = 1.50653 kg/m3

h Value = 537143 J/kg/K

Courant Number mean: 0.0145796 max: 0.0987648
deltaT = 2.43902e-05
Time = 0.0832439




Frederick

Last edited by rFkhemek; July 31, 2009 at 07:45.
rFkhemek is offline   Reply With Quote

Reply


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
Calculation of the Governing Equations Mihail CFX 7 September 7, 2014 06:27
Enquiry about the flame simulation in rotary kiln hassanelattar FLUENT 0 March 25, 2009 07:41
Adiabatic Flame Temperature Georg Main CFD Forum 1 November 28, 2008 07:35
Crosswind flame with reactingFoam torvic OpenFOAM Running, Solving & CFD 1 September 10, 2007 17:48
Flame temperature newbie Main CFD Forum 0 June 14, 2002 02:38


All times are GMT -4. The time now is 03:16.