-
-
December 16, 2024 at 2:34 pmll00023Subscriber
I used the Bilger's definition of mixture fraction to predict the coal combustion.Â
the volatile formula of PRB coal is C1.16H3.4O0.71N0.0741.
Since char combustion is a secondary factor to determine the coal flame, I only consider volatile flame here.
volatile contains nitrogen element, which doesn't affect the oxygen consumption; by referring Haifeng Wang 2023 's work, in the coupling function, nitrogen item could be eliminated.
so I can use eqn. 8.4-9 and 8.4-10.
the mixture fraction result is not showing Boundedness [0,1], Monotonicity. But stoichiometry preservation (0.146) is close to the flame location.
I assume this is due to the volatile release process. when using Eqn. 8.4-9, b_fuel - b_o = 2*Yc/Mc +0.5Yh/Mh+Yo/Mo, in which Yc = 0.148, Yh= 0.0361 from volatile , Yo=0.23 from oxidizer.
while for b, Yc is from the volatile in that cell, which is dependent upon the release process. I didn't find any solution for coal combustion.
how to make it right for coal combustion?
Thank you.
Â
Â
Â
-
December 18, 2024 at 3:26 pmRenAnsys Employee
Are you wanting to model coal combustion using Fluent? Which combusiton model are you considering? Why do you need to construct the Bilger mixture fraction?Â
Â
-
- You must be logged in to reply to this topic.
- How do I get my hands on Ansys Rocky DEM
- Non-Intersected faces found for matching interface periodic-walls
- Unburnt Hydrocarbons contour in ANSYS FORTE for sector mesh
- Help: About the expression of turbulent viscosity in Realizable k-e model
- Script Error
- Mass Conservation Issue in Methane Pyrolysis Shock Tube Simulation
- Facing trouble regarding setting up boundary conditions for SOEC Modeling
- convergence issue for transonic flow
- Running ANSYS Fluent on a HPC Cluster
- Point exception in erosion calculation
-
1882
-
802
-
599
-
591
-
366
© 2025 Copyright ANSYS, Inc. All rights reserved.