Theory
The program uses Sutherland's law (Sutherland, 1893) in the reference form of equation (1). It converts this to the two-constant form of equation (2), which OpenFOAM's sutherland transport model requires (OpenFOAM user guide, 2026): from equation (3) and . The same law provides the viscosity for:
- the incompressible solution (at the Material step's temperature);
- the heat-transfer correlations;
- the acoustic packing and perforate models.
makes the viscosity grow as (hard spheres). The packing flow resistivity, which is measured with room-temperature air, is scaled with the viscosity of this gas relative to that of air at 20 °C.
Equations
| where | meaning | unit |
|---|---|---|
| Dynamic viscosity | Pa s | |
| Viscosity at the reference temperature (entered in µPa s) | Pa s | |
| Reference temperature | K | |
| Sutherland temperature | K | |
| Sutherland coefficient | kg/(m s K^0.5) | |
| Sutherland temperature of the solver | K | |
| Temperature | K |
Default and rule
- Default
- 17.16 µPa s at 273.15 K, S = 110.4 K (air)
- Rule
A new material starts with the values for air: 17.16 µPa s at 273.15 K, = 110.4 K ( = 1.458e-6).
- Source
Sutherland's law (Sutherland, 1893) in the two-constant form of OpenFOAM's
sutherlandtransport model (OpenFOAM user guide, 2026).
Valid range mu_ref > 0; T_ref > 0; 0 <= S <= 5000 K
Typical S
Air 110.4 K, N₂ 111 K, CO₂ 240 K, helium about 79 K.
Fit range
Sutherland's law with one reference point is accurate over a few hundred kelvin around that point; choose the reference near the temperature of the run.