Re = ρVL/μ for flow over flat plates, aerofoils, cylinders, and spheres. Determines boundary-layer regime, drag behaviour, and flow separation.
Fluid Properties & StaticsCharacteristic length = plate length L measured from the leading edge.
Distance from leading edge
1 cP = 1 mPa·s = 0.001 Pa·s
Flat Plate — Air at 20°C, V = 10 m/s, L = 1 m
| Density ρ | 1.204 kg/m³ |
| Dynamic viscosity μ | 1.825×10⁻⁵ Pa·s |
| Plate length L | 1 m |
| Free-stream V∞ | 10 m/s |
Aerofoil — Air at 20°C, V = 30 m/s, chord c = 0.5 m
Cylinder — Water at 20°C, V = 0.5 m/s, D = 50 mm
Formula (same as internal flow, different characteristic length):
Regime thresholds by geometry:
| Geometry | Regime | Re range |
|---|---|---|
| Flat plate | Laminar BL | ReL < 5×10⁵ |
| Flat plate | Mixed BL (lam + turb) | 5×10⁵ ≤ ReL < 10⁷ |
| Flat plate | Turbulent BL (approx.) | ReL ≥ 10⁷ |
| Aerofoil | Ultra-low Re (insect/MAV) | Rec < 10⁴ |
| Aerofoil | Low Re — separation bubble | 10⁴ ≤ Rec < 10⁵ |
| Aerofoil | Transitional (glider/UAV) | 10⁵ ≤ Rec < 5×10⁵ |
| Aerofoil | High Re (classical aero) | Rec ≥ 5×10⁵ |
| Cylinder/Sphere | Creeping | Re < 1 |
| Cylinder/Sphere | Subcritical (laminar BL) | 1 ≤ Re < 2×10⁵ |
| Cylinder/Sphere | Critical (drag crisis) | 2×10⁵ ≤ Re < 5×10⁵ |
| Cylinder/Sphere | Supercritical | Re ≥ 5×10⁵ |
Flat plate / aerofoil — transition position:
The boundary layer is laminar for x < xcr and turbulent for x > xcr. Recr ≈ 5×10⁵ is the standard engineering value for a smooth surface with low free-stream turbulence. For aerofoils, xcr is expressed as a percentage of chord c.
Aerofoil — why Rec matters:
The transition position xtr is estimated using the flat-plate criterion Rex = 5×10⁵ — a useful approximation for zero-pressure-gradient sections. Actual xtr shifts forward with increasing angle of attack or adverse pressure gradient.
Cylinder drag crisis:
Around Re ≈ 2–5×10⁵ the laminar boundary layer trips to turbulent before separating, moving the separation point from ~80° to ~140° from the stagnation point. This dramatically narrows the turbulent wake and causes CD to drop from ~1.2 to ~0.3 — the so-called drag crisis. Golf ball dimples intentionally trigger this transition at lower Re to reduce drag in flight.
Where:
Viscosity Conversion
Fluid not in the presets? Convert μ and ν across all unit systems and cross-convert between the two using density.
Reynolds Number — Internal (Pipe) Flow
Same dimensionless number applied to flow inside circular pipes — different regime thresholds (Re < 2,300 laminar).
Boundary Layer Thickness
For flat plates and aerofoils: compute boundary layer thickness and skin-friction coefficient from local Re.
Drag on Sphere
For cylinders and spheres: calculate drag force from Re and the appropriate drag coefficient correlation.
Lift Force
For aerofoils: calculate lift force from lift coefficient, wing area, and dynamic pressure.