VERIFIED — law of the wall captured; Cf within ~9% of correlations
SolversimpleFoam + k–ω SST
Reynolds No.ReL = 10⁶
Mesh50,400 cells
Wall resolutiony⁺ = 0.12–0.31
Cf vs correlation~9% mean
TurbulenceRANS (first turbulent case)
1 Objective
Verify the digitalmodel CFD pipeline for turbulent flow — the regime of essentially all
real engineering CFD, and the first turbulent case in the validation suite (the flat-plate Blasius and
cylinder Re=100 cases are laminar). The test is the zero-pressure-gradient turbulent boundary layer,
whose near-wall structure obeys the universal law of the wall and whose skin friction follows
well-established empirical correlations.
skin friction Cf(Rex) ≈ 0.0592 Rex−1/5 (Prandtl) or (2 log₁₀ Rex − 0.65)−2.3 (Schlichting)
What this gates in real work
Real marine flows are turbulent — this case is the full-scale friction gate. A wall-resolved
k-ω SST boundary layer that lands on the universal law of the wall qualifies:
Ship & FPSO hull friction — full-scale Cf prediction and the ITTC/Schoenherr line
comparisons behind every powering estimate.
Appendage and rudder RANS — the same turbulence model, wall treatment (y⁺ ≈ 0.1–0.3,
no wall functions) and near-wall meshing used for lifting surfaces (see the NACA0012 case).
Current loads on hulls and jackets — drag coefficients used in mooring and DP capability
studies inherit their credibility from exactly this near-wall physics.
2 Primary result — the law of the wall
Velocity profile at Rex=10⁶ in wall units, normalised by the computed wall
friction velocity. The solution follows u⁺=y⁺ through the viscous sublayer, bends through the
buffer layer, and lies on the log law across the logarithmic region before lifting into the wake.
This is the definitive turbulence check. With the near-wall mesh resolved to
y⁺≈0.13 (viscous sublayer, no wall functions bridging the gap), the k–ω SST solution
reproduces all three canonical layers — sublayer, log law (κ≈0.41, B≈5.0), and wake.
A model that got the turbulent wall physics wrong could not collapse onto the universal profile.
3 Skin friction
Computed Cf(Rex) against the Prandtl and Schlichting turbulent correlations.
The comparison window (shaded) is the developed turbulent region Rex=5×10⁵–10⁶.
Metric
Value
Cf level at Rex=10⁶
0.00342 (vs 0.00375 correlation; ~5× the laminar Blasius value — unambiguously turbulent)
Mean |error| vs Schlichting (Rex 5×10⁵–10⁶)
9.3% (max 9.9%)
Trend
correct Cf ∝ Rex−1/5 decay
On the ~9% offset. The empirical turbulent correlations themselves scatter by
5–10% (Prandtl, Schlichting, White, Kármán–Schoenherr), and they assume a boundary layer
turbulent from the leading edge; the computed layer has a short resolved transition region near the
plate nose (visible as the larger deficit at low Rex, shrinking downstream). The self-consistent
law-of-the-wall collapse above — using the solution's own friction velocity — is the stronger and
more fundamental verification of the turbulence model; the skin-friction level agrees with the classical
correlations to within their own spread.
4 Numerical model
Item
Specification
Solver / model
simpleFoam + kOmegaSST (RANS), steady, SIMPLEC
Domain / mesh
Two-block: 0.2 m symmetry run-in + 1.0 m plate, H=0.3 m; 50,400 cells; wall-normal grading to y⁺=0.12–0.31 (sublayer-resolved, low-Re wall treatment)
Flow
U∞=1, ν=10⁻⁶ → ReL=10⁶
Wall BCs
k kLowReWallFunction, ω omegaWallFunction, νtnutLowReWallFunction
Verification
y⁺ via the yPlus function object; Cf from wallShearStress; u⁺ profile normalised by the local computed uτ
5 Conclusion
Verified. The digitalmodel CFD pipeline reproduces a wall-resolved turbulent
boundary layer with the k–ω SST model: the velocity profile collapses onto the universal law of
the wall (sublayer + log law + wake) at y⁺≈0.13, and the skin friction matches the classical
turbulent correlations to within ~9% (their own mutual scatter). This extends the verified
capability from laminar (flat-plate Blasius, cylinder Re=100) to turbulent RANS — the regime
of practical engineering CFD.
References
Schlichting, H. & Gersten, K. (2017). Boundary-Layer Theory, 9th ed., Springer.
White, F. M. (2006). Viscous Fluid Flow, 3rd ed., McGraw-Hill.
Menter, F. R. (1994). "Two-equation eddy-viscosity turbulence models for engineering applications." AIAA J. 32(8), 1598–1605.
NASA Turbulence Modeling Resource — 2D zero-pressure-gradient flat plate.