|February 4, 2012, 07:13||
Too low temperature at combustor outlet
Join Date: Nov 2011
Posts: 4Rep Power: 6
I have problem with my CFD simulation. I have to model a combustion process in turbine engine combustor.
Here are some information about simulation:
ANSYS Fluent 13.0
- pressure based
- realizable k-epsilon
- partially premixed combustion of c12h23
- DPM with 4 continuous phase iterations per DPM iteration, other properties defaults.
- Cone injection, droplet, kerosene-liquid, evaporating species: c12h23
- mesh is 5 mln tetra (I also tried 6 and 20 mln tetra, but final problem was always the same)
I run calculations in 3 steps:
1. Calculating only air flow
2. Turning on DPM
3. Calculating combustion by patching progress variable equal 1 to whole combustor.
Im monitoring temperature at combustor outlet (t_min, t_mean and t_max).
Calculated and experimentally measured average temperature (t_mean) at outlet is about 1180K
Problem starts when I "ignite" mixture.
After some iterations temperature "is trying" to converge at 1180K - great! ( temperature distribution in whole chamber is also correct )
but after more iterations, temperature drops to value of about 600K. Temperature distribution in chamber is also not good then.
It is clearly shown at plots of residuals and outlet temperature.
Here are some info from FLUENT:
iter continuity x-velocity y-velocity z-velocity energy k epsilon fmean fvar premixc t_max t_mean t_min time/iter 1628 2.4042e-03 1.7096e-04 2.8642e-04 1.6927e-04 1.0230e-04 1.8258e-04 5.7209e-04 9.0740e-05 3.4400e-04 4.9054e-05 6.3157e+02 6.1549e+02 5.9406e+02 2:22:29 549 turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 98345 cells 1629 3.9247e-03 1.6888e-04 2.0046e-04 1.6883e-04 5.1275e-05 1.3198e-04 4.2686e-04 5.5448e-05 1.9339e-04 4.4105e-05 6.3146e+02 6.1542e+02 5.9401e+02 2:30:19 548 turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 96157 cells 1630 4.6650e-03 5.5767e-04 6.3399e-04 5.5584e-04 4.6992e-05 1.4767e-04 3.7893e-04 5.4586e-05 1.6977e-04 4.3964e-05 6.3145e+02 6.1549e+02 5.9421e+02 2:23:44 547 turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 97903 cells 1631 3.3313e-03 2.9818e-04 3.3710e-04 2.9924e-04 7.1853e-05 1.6899e-04 5.4183e-04 6.5568e-05 2.7728e-04 4.7080e-05 6.3134e+02 6.1541e+02 5.9416e+02 2:20:16 546 DPM Iteration .... turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 98144 cells number tracked = 100, escaped = 0, aborted = 0, trapped = 0, evaporated = 100, incomplete = 0, incomplete_parallel = 0 Parallel particle tracking concurrency: 12% 1632 2.2688e-03 1.8252e-04 2.2522e-04 1.8308e-04 1.0133e-04 1.8126e-04 5.7111e-04 8.9342e-05 3.4547e-04 4.8546e-05 6.3124e+02 6.1534e+02 5.9411e+02 2:19:15 545 turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 97101 cells 1633 2.8380e-03 9.6682e-05 1.3500e-04 9.7134e-05 4.6253e-05 1.2884e-04 4.1273e-04 5.0446e-05 1.8599e-04 4.3897e-05 6.3113e+02 6.1526e+02 5.9406e+02 2:27:28 544 turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 93080 cells 1634 4.1602e-03 5.3542e-04 6.1055e-04 5.2838e-04 3.5126e-05 1.4833e-04 3.7456e-04 4.7603e-05 1.4393e-04 4.2551e-05 6.3155e+02 6.1568e+02 5.9448e+02 2:21:17 543 turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 94129 cells 1635 4.0336e-03 3.2497e-04 3.8269e-04 3.2224e-04 7.5555e-05 1.7263e-04 5.2619e-04 6.7395e-05 2.8646e-04 4.7405e-05 6.3145e+02 6.1560e+02 5.9444e+02 2:23:32 542 DPM Iteration .... turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 95817 cells number tracked = 100, escaped = 0, aborted = 0, trapped = 0, evaporated = 100, incomplete = 0, incomplete_parallel = 0 Parallel particle tracking concurrency: 11%
I changed turbulent viscosity ratio limit from 1e5 to 2.5e5, and decreased turbulent relaxation factors. Also increased turbulent intensity in boundary conditions from 5 to 10%. Information "turbulent viscosity limited to..." disappeared, but now I have information that
Minimum PDF table temperature in xxxx cells on zone 2...
I think that it also might be problem with viscosity. In mixture properties viscosity is set to be temperature dependent. But on the plots, I get constant value of mentioned property ( about 1.51 e-5 )
I'm trying many variants, but all of them takes a lot of time... I'd be really grateful for any help
|February 6, 2012, 11:02||
Join Date: Nov 2011
Posts: 4Rep Power: 6
xrs333 thank you for answer
PDF was ok. Problem was with combustion model. Not partially premixed, but non-premixed.
I have changed, and now it's ok.
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