-
-
May 24, 2024 at 6:12 pmdkmenendSubscriber
Hello,
I am running a 2d invicid case with all walls (no inlet or outlet). The cell size is a 0.05mm and the tube length is 100m, height is 20mm. The left 20mm of the tube is patched to have all hydrogen, the remaining 80mm to the right is patched to have a mole frac of 0.11 and 0.89 of h2 and o2 repsectively. I am using volumetric species transport model 1 step reaction with stiff chmeistry solver default settings.
I calculated CFL to be 0.02 based off a previous study in which the shock velocity was 1km/s. My time step is 1e-9s and cell length is 0.05mm
I am getting very bad convergence pictured below. I do not know what is causing this. An additional problem is that the contour map of mass fraction of h2 does not change as time goes on. I would expect this to change as reaction rate clearly shows a reaction occouring.
-
May 24, 2024 at 6:15 pmdkmenendSubscriber
I forgot to include that the left side was patched to 100,000pa as well. Also the picture of the mass fraction of h2 did not upload correctly so i have placed it here.
Another piece of information is that I get the "divergence detected, reducing courant number to 0.002" at each interation as well as the
"corrections zeroed in 1468 cells due to excessive temperature change"
-
May 29, 2024 at 5:05 pmPrashanthAnsys Employee
Hello: Are you able to converge the solution without species and reactions enabled, say with just high and low pressure hydrogen in shock tube?
-
- The topic ‘Hydrogen Air Shocktube’ is closed to new replies.
- 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
- Cyclone (Stairmand) simulation using RSM
- error udf
- Diesel with Ammonia/Hydrogen blend combustion
- Fluent fails with Intel MPI protocol on 2 nodes
- Mass Conservation Issue in Methane Pyrolysis Shock Tube Simulation
- Script error Code: 800a000d
- Encountering Error in Heterogeneous Surface Reaction
-
1191
-
513
-
488
-
225
-
209
© 2024 Copyright ANSYS, Inc. All rights reserved.