The Rayleigh number is a dimensionless quantity that helps you decide whether heat transfer in a fluid layer is dominated by pure conduction or by buoyancy-driven natural convection. It compares how strongly warm, light fluid wants to rise (buoyancy) against how much viscosity and thermal diffusion resist motion and smooth out temperature differences.
In practical terms, a low Rayleigh number indicates that the fluid remains almost motionless and heat flows mainly by conduction. A high Rayleigh number indicates that buoyancy overcomes viscous and diffusive effects, so convection cells form and heat transfer becomes much more efficient.
For a horizontal layer of fluid heated from below, a commonly used definition of the Rayleigh number is:
Using standard notation, this can also be written in plain text as:
Ra = (g · β · ΔT · L³) / (ν · α)
The numerator g β ΔT L³ represents the driving buoyancy forces caused by thermal expansion in a gravitational field. The denominator ν α represents how viscosity and thermal diffusion suppress temperature differences and fluid motion.
The calculator is designed around the standard Rayleigh number formula. To compute Ra for your case:
Once these values are entered, the calculator evaluates Ra using the formula above and displays the dimensionless Rayleigh number.
The magnitude of Ra tells you how important natural convection is in your system:
For the classic case of a horizontal fluid layer with rigid, isothermal boundaries, linear stability theory predicts a critical Rayleigh number of approximately:
Racritical ≈ 1708
Below this threshold, the conduction state is stable; above it, convection sets in. However, this critical value is not universal. It changes with boundary conditions (rigid vs. free surfaces), heating direction (bottom vs. top), and geometry (vertical plates, enclosures, spherical shells, and so on).
This example shows how to go from physical inputs to a numerical Rayleigh number using the calculator.
Problem: A horizontal layer of water is heated from below. The layer is 0.02 m thick (2 cm). The bottom is 10 K (or 10 °C) hotter than the top. Estimate the Rayleigh number at room temperature.
Given data (approximate properties at 20–25 °C):
Step 1: Compute L³
L³ = (0.02 m)³ = 8.0 × 10−6 m³
Step 2: Compute the numerator g β ΔT L³
g β ΔT L³ = (9.81) × (2.5 × 10−4) × (10) × (8.0 × 10−6)
First combine the numerical factors: 9.81 × 2.5 × 10 × 8.0 ≈ 1962
Now combine powers of ten: 10−4 × 10−6 = 10−10
So the numerator ≈ 1.962 × 103 × 10−10 = 1.962 × 10−7
Step 3: Compute the denominator ν α
ν α = (1.0 × 10−6) × (1.4 × 10−7) = 1.4 × 10−13 m⁴/s²
Step 4: Take the ratio to find Ra
Ra = (1.962 × 10−7) / (1.4 × 10−13)
First divide the coefficients: 1.962 / 1.4 ≈ 1.40
Then subtract exponents: 10−7 / 10−13 = 106
So Ra ≈ 1.40 × 106
Interpretation: Ra ≈ 1.4 × 106 is far above the critical value of 1708 for a horizontal water layer. This indicates vigorous natural convection and a transition to convection-dominated heat transfer. In a real experiment, you would expect to see convection cells or plumes forming in the fluid.
The Rayleigh number is closely connected to several other dimensionless groups used in heat transfer and fluid mechanics. In fact, it can be written as the product of the Grashof and Prandtl numbers:
Ra = Gr · Pr
| Number | Definition | Main role | Relation to Rayleigh number |
|---|---|---|---|
| Rayleigh (Ra) | (g β ΔT L³) / (ν α) | Measures balance of buoyancy vs. viscous and thermal diffusion effects in natural convection. | Key parameter for onset and intensity of natural convection; equals Gr × Pr. |
| Grashof (Gr) | (g β ΔT L³) / ν² | Ratio of buoyancy forces to viscous forces. | Ra = Gr × Pr, so Gr describes fluid motion tendency without considering thermal diffusivity. |
| Prandtl (Pr) | ν / α | Ratio of momentum diffusivity to thermal diffusivity. | Determines relative thickness of velocity and thermal boundary layers; multiplies with Gr to form Ra. |
| Nusselt (Nu) | h L / k | Ratio of convective to conductive heat transfer at a surface. | Often correlated as Nu = f(Ra, Pr) in natural convection correlations. |
| Reynolds (Re) | U L / ν | Ratio of inertial to viscous forces; characterizes forced convection flows. | Not directly in the Ra formula, but important when both natural and forced convection are present. |
In many engineering correlations for natural convection, the Nusselt number is given as a function of the Rayleigh (and sometimes Prandtl) number. That is why calculating Ra is often the first step toward estimating heat transfer coefficients.
Different physical systems fall into characteristic Rayleigh number ranges:
The calculator is well suited for small-to-medium scale engineering problems, such as assessing whether a cavity or enclosure will experience significant natural convection or remain conduction dominated.
The standard Rayleigh number formula and this calculator rely on several simplifying assumptions. Being explicit about these helps you judge whether the result applies to your situation:
The calculator itself simply evaluates the Rayleigh number formula. It does not automatically choose correlations or predict Nusselt number, heat transfer coefficients, or temperature profiles. For design work, you should combine the computed Rayleigh number with appropriate correlations or simulations and engineering judgment.
No. The Grashof number (Gr) measures the ratio of buoyancy to viscous forces: Gr = (g β ΔT L³) / ν². The Rayleigh number multiplies Gr by the Prandtl number (Pr = ν/α), giving Ra = Gr · Pr. Rayleigh therefore incorporates both momentum and thermal diffusivity.
For a horizontal fluid layer heated from below, bounded by rigid and isothermal surfaces, the theoretical critical value is about Ra ≈ 1708. However, in other geometries (vertical enclosures, free surfaces, complex boundaries), the critical Rayleigh number can be higher or lower. Use the 1708 threshold only when your configuration closely matches the classic Rayleigh–Bénard problem.
Yes. The formula applies to any single-phase fluid, provided you use appropriate property values for β, ν, and α at your operating temperature and the density variations satisfy the Boussinesq approximation. It is commonly used for air and water, but also for oils, refrigerants, and other engineering fluids.
Not directly, because Ra is dimensionless and formulated in terms of material properties and temperature differences. However, the fluid properties (β, ν, α) do depend on temperature and pressure. If your system operates at high pressure, you must obtain the correct property data before calculating Ra.
Once you know Ra, you can:
Used carefully, the Rayleigh number is a compact way to organize and compare a wide variety of convection problems.
Enter positive values in consistent SI units. Viscosity and diffusivity are often on the order of 10⁻⁷ to 10⁻⁵ m²/s for liquids and gases.