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Convective coefficient at the surface
V / As of the body
Conductivity of the solid material
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About

The Biot number Bi is a dimensionless ratio comparing the conductive resistance inside a solid body to the convective resistance at its surface. It is defined as Bi = h Lc ÷ k, where h is the convective heat transfer coefficient W/(m2⋅K), Lc is the characteristic length m, and k is the solid's thermal conductivity W/(m⋅K). When Bi < 0.1, the internal temperature gradient is negligible and the lumped capacitance method applies. This simplifies transient conduction analysis from a partial differential equation to an ordinary one. Getting this threshold wrong leads to errors exceeding 5% in predicted cooling or heating times, which matters in quench-hardening steel, food safety pasteurization, and electronics thermal management.

This calculator accepts direct inputs or computes Lc = V ÷ A from standard geometries (plane wall, long cylinder, sphere). The tool approximates steady boundary conditions and uniform h. For geometries with non-uniform convection or internal heat generation, a full finite-element approach is required. Pro tip: in forced convection scenarios, always verify h against published correlations for your flow regime before trusting a lumped analysis.

biot number heat transfer lumped capacitance thermal conductivity convection thermodynamics Bi number

Formulas

The Biot number is defined as the ratio of internal conductive resistance to external convective resistance at the surface of a body:

Bi = h Lck

Where h = convective heat transfer coefficient W/(m2⋅K), Lc = characteristic length m, k = thermal conductivity of the solid W/(m⋅K).

The characteristic length Lc is the ratio of the body's volume to its surface area:

Lc = VAs

For standard geometries this simplifies to:

{
Plane wall (half-thickness): Lc = L2Long cylinder: Lc = r2Sphere: Lc = r3

Lumped capacitance criterion: if Bi < 0.1, the temperature within the body can be assumed spatially uniform during transient heat transfer. This reduces the governing PDE to an exponential decay ODE with time constant τ = ρ cp Vh As.

Reference Data

MaterialThermal Conductivity k W/(m⋅K)Typical Bi Range (forced air)
Copper (pure)4010.0001 - 0.004
Aluminum 60611670.001 - 0.01
Carbon Steel AISI 101049.80.003 - 0.05
Stainless Steel 30414.90.01 - 0.2
Titanium Ti-6Al-4V6.70.02 - 0.5
Silicon1480.001 - 0.01
Glass (soda-lime)1.00.1 - 5.0
Brick (common)0.720.15 - 7.0
Concrete1.40.08 - 3.5
Oak Wood0.170.5 - 30
Nylon 6,60.250.4 - 20
PTFE (Teflon)0.250.4 - 20
Rubber (natural)0.130.8 - 40
Water (liquid, 25°C)0.607 -
Air (25°C, 1 atm)0.026 -
Gold3170.0002 - 0.005
Nickel90.70.002 - 0.02
Lead35.30.004 - 0.07
Polycarbonate0.200.5 - 25
Granite2.790.04 - 1.8

Frequently Asked Questions

At Bi < 0.1, the maximum temperature difference inside the body is less than 5% of the total temperature difference between the body center and the surrounding fluid. This was established through exact series solutions to the heat equation for canonical shapes (Heisler charts). Beyond 0.1, spatial gradients become significant and the assumption of uniform body temperature introduces unacceptable error.
The standard definition uses Lc = V ÷ As. Some textbooks (notably Incropera) use half-thickness for a plane wall, giving Lc = L. This doubles the Biot number compared to the V÷A definition. Always confirm which definition your reference uses before comparing results. This calculator uses the V÷A convention for geometry presets.
No. The Biot number specifically describes conduction within a solid relative to convection at its surface. For fluid-to-fluid scenarios, the relevant dimensionless group is the Nusselt number Nu = hL÷kfluid, which uses the fluid's thermal conductivity rather than the solid's. Confusing Bi and Nu is a common error in undergraduate courses.
When Bi >> 1, internal resistance dominates. The surface temperature approaches the fluid temperature almost immediately, while the interior lags. This is the regime for thick, poorly conducting bodies like large ceramic components or food items during cooking. In this regime, the temperature profile is solved using Heisler charts or the full Fourier series solution.
The coefficient h depends on flow conditions, fluid properties, and geometry. For natural convection in air, typical values range from 5 to 25 W/(m2⋅K). Forced air gives 25 - 250 W/(m2⋅K). Water convection ranges from 100 to 20,000 W/(m2⋅K). Use empirical correlations (Dittus-Boelter for internal turbulent flow, Churchill-Chu for natural convection on vertical plates) to calculate h for your specific conditions.
No. The Biot number as defined here considers only convective resistance at the surface. If radiative heat loss is significant (high surface temperatures, low convection), you must compute a combined coefficient heff = hconv + hrad and use that value in the calculator. The linearized radiation coefficient is hrad 4εσTm3, where Tm is the mean temperature.