Richardson number#
Named after: Lewis Fry Richardson (1881-1953).
$$\text{Ri} \stackrel{\text{def}}{=} \frac{g \beta (T_s - T_\infty) L}{U^{2}} \sim \frac{\text{buoyancy}}{\text{inertia}}$$
Description#
Measures buoyancy relative to inertial forcing. It indicates whether a flow behaves more like forced, mixed, or natural convection.
Quantities#
| Name | Symbol | SI units | Dimension |
|---|---|---|---|
| gravitational acceleration | \(g\) | \(\mathrm{m}\,\mathrm{s}^{-2}\) | \(\text L\,\text T^{-2}\) |
| thermal expansion coefficient | \(\beta\) | \(\mathrm{K}^{-1}\) | \(\Theta^{-1}\) |
| surface-ambient temperature difference | \(T_s - T_\infty\) | \(\mathrm{K}\) | \(\Theta\) |
| characteristic length | \(L\) | \(\mathrm{m}\) | \(\text L\) |
| velocity | \(U\) | \(\mathrm{m}\,\mathrm{s}^{-1}\) | \(\text L\,\text T^{-1}\) |
Regimes#
Mixed convection
| Range | Regime | Description |
|---|---|---|
| 0 – 0.25 | forced convection | Inertial forcing dominates buoyancy. Temperature differences have a weak effect on the main flow. |
| 0.25 – 1 | mixed convection | Buoyancy and imposed motion both influence the flow and heat-transfer pattern. |
| 1 – ∞ | natural convection | Buoyancy dominates over imposed inertia. Flow structure is set mainly by density differences. |