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Gaspar García, CFD portfolio

Impinging jet: a transition model does not fix the stagnation region

ComparedUpdated 2026-11-14

Objective. Predict wall heat transfer under a round turbulent jet impinging on a heated plate, and test whether a transition model recovers the secondary Nusselt peak that fully turbulent RANS misses.

Parameters
Reynolds number (bulk velocity, nozzle diameter)23,000
Nozzle-to-plate distance H/D2
Nozzle diameter D0.1016 m
Bulk velocity3.48857 m/s
FluidAir: density 1.18816 kg/m³, viscosity 1.831e-05 Pa s, Prandtl number 0.705
SolverOpenFOAM v2412, buoyantSimpleFoam with gravity off (forced convection)
Turbulence modelk-omega SST; Langtry-Menter k-omega SST-LM on the identical mesh
Wall treatmentWall-resolved: plate first cell 20 µm, y+ max 0.23
Geometry view
1 Geometry
Mesh view
2 Mesh
Results view
3 Results

Comparison with experiment

QuantityExperimentSSTSST, signedSST-LMSST-LM, signed
Nu error at stagnation, r/D 00.12230.1384+13 %0.1419+16 %
Nu error at the secondary peak, r/D 1.940.09410.0881−6 % (no peak)0.0860−9 % (no peak)
Nu error in the wall jet, r/D 2.5 and beyond––−4.3 to +0.4 %–−1.5 to +4.3 %
Mean |error|, all stations––12.3 %–12.2 %

Nu / Re^0.7 against r/D

0.050.0750.10.125024r/DNu / Re^0.7
  • Experiment (Baughn et al. 1992)
  • k-omega SST
  • k-omega SST-LM

Verdict

k-omega SST gets the developed wall jet right and over-predicts stagnation heat transfer by +13 %. The transition model gives the same mean error and no secondary peak, so the simpler model stays.

Limits

  • Single grid: no numerical uncertainty band.
  • Experimental Nu uncertainty is not stated in the source.
  • SST ran 4000 iterations against 8000 for SST-LM, so the mean-error tie is unresolved.