Theory
The model solves two transport equations, one for the turbulent kinetic energy , equation (1), and one for its specific dissipation rate , equation (2) (Menter, 1994). A blending function switches the model from the k-ω form near walls, which needs no damping functions and works down to the wall, to a k-ε-like form in the free stream, which removes the k-ω model's sensitivity to the free-stream . The eddy viscosity is limited by the strain rate, equation (3) (the "shear-stress transport" limiter), which improves separated flows: the jets and recirculation zones of a muffler.
At walls the program uses wall functions or a resolved wall (Wall treatment): Spalding's law for with the log-law constants and () (Spalding, 1961). The inlet values of and come from the turbulence intensity and length scale of the inlet (Turbulence intensity).
The model constants are OpenFOAM's defaults, which are Menter's standard set; the program does not change them.
Equations
| where | meaning | unit |
|---|---|---|
| Turbulent kinetic energy | m²/s² | |
| Specific dissipation rate | 1/s | |
| Density (constant for incompressible) | kg/m³ | |
| Mean velocity | m/s | |
| Effective diffusivities, and | m²/s | |
| Production of by the mean shear | m²/s³ | |
| Eddy viscosity | m²/s | |
| Strain-rate magnitude | 1/s | |
| Blending functions (1 near walls, 0 far away) | - | |
| Blended constants: 0.85 / 1.0, 0.5 / 0.856, 0.075 / 0.0828, 5/9 / 0.44 (inner / outer) | - | |
| 0.09, 0.31, 1, 10 | - |
Default and rule
- Default
- k-ω SST
- Rule
k-ω SST with OpenFOAM's default constants.
- Source
Menter's SST model (Menter, 1994) as implemented in OpenFOAM (OpenFOAM user guide, 2026). The production limiter with and the form of the cross-diffusion term follow OpenFOAM's implementation, which is based on a later revision of the model by Menter and co-workers. Wall-function constants: see Wall treatment.
Valid range k-ω SST only
Fixed
No other turbulence model is offered. Laminar flow is not modelled: the setup check warns when an inlet Reynolds number is below 2300, where the model adds an eddy viscosity a laminar flow does not have.
Related 6
References 3
- Menter, F. R. (1994). Two-equation eddy-viscosity turbulence models for engineering applications. AIAA Journal, 32(8), 1598-1605. DOI 10.2514/3.12149
- OpenCFD Ltd. (2026). OpenFOAM user guide. openfoam.com. Web page
- Spalding, D. B. (1961). A single formula for the law of the wall. Journal of Applied Mechanics, 28(3), 455-458. DOI 10.1115/1.3641728