Nusselt Number
The Nusselt number (Nu) is the ratio of convective to conductive heat transfer. Nu = hL/k links heat transfer coefficient h to fluid conductivity k and characteristic length L.
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Nu < 1: conduction dominant; Nu 10–100: typical forced convection Dittus-Boelter for turbulent pipe: Nu = 0.023 Re^0.8 Pr^n Natural convection: Nu ∝ Ra^1/4 (laminar) or Ra^1/3 (turbulent) Characteristic length L: plate length, pipe diameter, or cylinder diameter
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Why: Nusselt number predicts convective heat transfer in heat exchangers, cooling systems, and thermal design. Higher Nu means stronger convection.
How: Direct: Nu = hL/k. Correlations use Re and Pr for forced convection, Ra or Gr for natural convection. Geometry-specific (flat plate, pipe, cylinder, sphere).
Run the calculator when you are ready.
🌬️ Flat Plate Forced Convection
Air flowing over a heated flat plate - turbulent flow
💧 Pipe Flow - Water
Water flowing through a heated pipe - turbulent flow (Dittus-Boelter)
🔥 Natural Convection Vertical Plate
Natural convection from a hot vertical plate in air
🌀 Cylinder in Cross-Flow
Air flowing across a heated cylinder
⚪ Sphere in Fluid
Natural convection around a heated sphere in water
Nusselt Number Inputs
Frequently Asked Questions
What is the Nusselt number?
The Nusselt number (Nu) is a dimensionless parameter that represents the ratio of convective to conductive heat transfer across a boundary. It's defined as Nu = hL/k, where h is the convective heat transfer coefficient, L is the characteristic length, and k is the thermal conductivity of the fluid.
What is a good Nusselt number?
Nusselt number values vary significantly based on flow conditions:
- Nu < 1: Very low (conduction dominant)
- Nu 1-10: Low (natural convection typical)
- Nu 10-100: Moderate (forced convection typical)
- Nu 100-1000: High (strong forced convection)
- Nu > 1000: Very high (boiling/condensation)
What is the difference between forced and natural convection?
Forced convection occurs when fluid motion is driven by external means (fans, pumps, wind), typically resulting in higher Nusselt numbers (10-1000+). Natural convection occurs due to buoyancy forces from temperature differences, typically resulting in lower Nusselt numbers (1-100). Natural convection correlations use Rayleigh or Grashof numbers, while forced convection uses Reynolds and Prandtl numbers.
What is the Dittus-Boelter equation?
The Dittus-Boelter equation is a widely used correlation for turbulent flow in circular pipes: Nu = 0.023 × Re^0.8 × Pr^n, where n = 0.4 for heating and n = 0.3 for cooling. It's valid for Re > 10,000 and 0.7 < Pr < 160. This correlation is fundamental in heat exchanger design and thermal system analysis.
How do I choose the right correlation?
Select correlations based on: (1) Geometry (flat plate, pipe, cylinder, sphere), (2) Flow type (forced vs natural), (3) Flow regime (laminar vs turbulent based on Re or Ra), and (4) Validity ranges. Always verify that your Reynolds, Prandtl, Rayleigh, and Grashof numbers fall within the correlation's specified validity range for accurate results.
What is the characteristic length?
The characteristic length (L) is a representative dimension used to define the Nusselt number. It depends on geometry:
- Flat plate: Length in flow direction
- Pipe: Diameter
- Cylinder: Diameter
- Sphere: Diameter
- Vertical plate: Height
How does Prandtl number affect Nusselt number?
The Prandtl number (Pr) represents the ratio of momentum diffusivity to thermal diffusivity. Higher Pr values (e.g., oils, Pr ≈ 100-10,000) indicate slower thermal diffusion relative to momentum, typically resulting in higher Nusselt numbers for the same Reynolds number. Lower Pr values (e.g., liquid metals, Pr ≈ 0.01-0.1) indicate faster thermal diffusion.
Official Data Sources
All heat transfer correlations and fluid properties are verified against authoritative engineering references:
Engineering Toolbox
Nusselt number correlations and convection reference
https://www.engineeringtoolbox.com/Last Updated: 2026-02-07
MIT OpenCourseWare
Heat transfer lecture materials
https://ocw.mit.edu/courses/mechanical-engineering/Last Updated: 2026-02-07
NIST Thermophysical Properties
Standard reference for fluid thermal properties
https://webbook.nist.gov/Last Updated: 2026-02-07
Incropera Heat Transfer
Fundamentals of Heat and Mass Transfer textbook
https://www.wiley.com/Last Updated: 2025-12-01
⚠️ Disclaimer
Engineering Use Disclaimer:
This calculator provides estimates based on empirical correlations and should be used for educational and preliminary design purposes only. Actual heat transfer coefficients may vary significantly due to:
- Surface roughness and geometry variations
- Fluid property variations with temperature
- Entry effects and developing flow conditions
- Boundary conditions and wall temperature distributions
- Correlation validity range limitations
For critical applications: Consult qualified thermal engineers, verify correlations against experimental data, perform sensitivity analysis, and consider safety factors. Always validate results with experimental measurements or validated CFD simulations for production systems.
For educational and informational purposes only. Verify with a qualified professional.
🔬 Physics Facts
Nu = 1 for pure conduction; convection increases Nu
— Heat Transfer
Dittus-Boelter (1930) remains standard for turbulent pipe flow
— Incropera
Churchill-Chu correlations cover Ra from 10^-6 to 10^12
— Churchill & Chu
Pr = μcp/k; water Pr≈7, air Pr≈0.7, oils Pr>100
— Fluid Properties
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