Nusselt Number Calculator

Calculate the Nusselt number, Reynolds, Prandtl, heat transfer coefficient for pipe flow and flat plate using Dittus-Boelter and Gnielinski correlations.

Nusselt Number
397.150
Correlation: Dittus-Boelter
Reynolds Number
74,850
Regime: Turbulent
Prandtl Number
6.993
Pr = µCp/k
Péclet Number
523,449
Pe = Re·Pr
Heat Transfer Coeff
4,749.91 W/m²·K
h = Nu·k/L
Flow Regime
Turbulent
Re > 10000

Flow Regime

Laminar
Transition
Turbulent

Nusselt Number Correlations

CorrelationFormulaRangeApplication
Dittus-BoelterNu = 0.023·Re^0.8·Pr^0.4Re > 10000, 0.6 < Pr < 160Turbulent pipe flow (heating)
Sieder-TateNu = 0.027·Re^0.8·Pr^(1/3)(µ/µw)^0.14Re > 10000Turbulent with viscosity variation
GnielinskiNu = (f/8)(Re−1000)Pr/[1+12.7√(f/8)(Pr^(2/3)−1)]2300 < Re < 5×10⁶Transitional & turbulent pipe
Flat plate (laminar)Nu = 0.332·Re^0.5·Pr^(1/3)Re < 5×10⁵External laminar flow
Flat plate (turbulent)Nu = 0.0296·Re^0.8·Pr^(1/3)Re > 5×10⁵External turbulent flow
Planning notes, formulas, and examples

About the Nusselt Number Calculator

The Nusselt number (Nu) is the dimensionless ratio of convective to conductive heat transfer at a surface. It tells you how effectively a flowing fluid transfers heat compared to pure conduction through a stagnant layer. Higher Nu means better convective heat transfer.

This calculator computes Nu using appropriate correlations based on flow regime and geometry. For pipe flow, it uses the constant Nu = 3.66 (laminar), Gnielinski correlation (transitional), or Dittus-Boelter (turbulent). For external flat plate flow, it applies laminar or turbulent boundary layer correlations.

Along with Nu, the calculator determines Re (Reynolds number), Pr (Prandtl number), Pe (Péclet number), and the convective heat transfer coefficient h = Nu·k/L. Preset buttons load fluid properties for water, air, oil, and coolant to speed up calculations. A reference table lists five common Nusselt correlations with their formulas, ranges, and applications.

Engineers use the Nusselt number for heat exchanger design, cooling system analysis, HVAC calculations, and any scenario involving forced convection heat transfer.

When This Page Helps

The Nusselt number is the gateway to computing convective heat transfer coefficients, which are essential for heat exchanger sizing, cooling system design, and thermal management.

This calculator automatically selects the correct correlation based on flow conditions, saving you from having to remember which formula applies in each regime. It is especially useful when you need a quick engineering estimate for heat exchangers, ducts, or cooling loops without cross-checking multiple textbooks.

How to Use the Inputs

  1. Select the geometry: pipe (internal flow) or flat plate (external flow).
  2. Enter the characteristic length (pipe diameter or plate length) in meters.
  3. Enter the fluid velocity, viscosity, density, specific heat, and thermal conductivity.
  4. Read the Nusselt number, Reynolds number, Prandtl number, and heat transfer coefficient.
  5. Use preset buttons to load fluid properties for common fluids.
  6. Check which correlation was used in the reference table.
Formula used
Dittus-Boelter: Nu = 0.023·Re^0.8·Pr^0.4 (Re > 10000). Gnielinski: Nu = (f/8)(Re−1000)Pr / [1 + 12.7√(f/8)(Pr^(2/3)−1)]. Laminar pipe: Nu = 3.66 (constant Tw, fully developed). h = Nu·k/L. Re = ρVL/µ, Pr = µCp/k.

Example Calculation

Result: Re = 74,850, Pr = 6.99, Nu = 377, h = 4,510 W/m²·K

Re = 998×1.5×0.05/0.001 = 74,850 (turbulent). Pr = 0.001×4182/0.598 = 6.99. Dittus-Boelter: Nu = 0.023×74850^0.8×6.99^0.4 = 377. h = 377×0.598/0.05 = 4,510 W/m²·K.

Tips & Best Practices

  • For water at room temperature, Pr ≈ 7. For air, Pr ≈ 0.71. For oils, Pr can exceed 1000.
  • Increasing velocity increases Re and Nu, but also increases pumping power (∝ V³).
  • In the laminar regime, Nu is nearly independent of Re — increasing flow speed barely helps.
  • The transition region (2300 < Re < 10000) is unstable — design to be clearly laminar or clearly turbulent.
  • For non-circular ducts, use the hydraulic diameter Dh = 4A/P as the characteristic length.

Choosing a Correlation

The right correlation depends on geometry and flow regime. A pipe with fully developed turbulent flow uses a different relation than a flat plate or a transitional internal flow. The calculator's preset logic helps avoid applying a turbulent formula where the assumptions are not met.

What to Compare

Nu is most valuable when you compare one fluid, diameter, or velocity against another. A higher value means stronger convection, but it does not mean the system is automatically better overall because pressure drop usually rises at the same time.

How to Use the Output

Use the heat transfer coefficient to size equipment, then check the Reynolds and Prandtl numbers to see whether the chosen model is credible. That keeps the result tied to the actual thermal design problem instead of treating Nu as a standalone score.

Sources & Methodology

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Frequently Asked Questions

  • High Nu means convection dominates over conduction — heat is being transferred very effectively by the fluid flow. Turbulent flows have much higher Nu than laminar flows.