Peclet Number Calculator

Fast Peclet estimates show when flow dominates over diffusion in systems today. Switch heat or mass modes, validate inputs, and download reports instantly here.

Inputs

Pick thermal or species transport.
Use known dimensionless groups if available.
Choose L that matches the gradient length.
Mean flow speed along transport direction.
Characteristic distance for diffusion to act.
Useful when you have material properties.
Typical water: ~1.4×10⁻⁷ m²/s.
Dimensionless-group helpers (optional)
Use these if you selected Reynolds-group method, or want extra context.
U = m/s, L = m
SI: U = m/s, L = m
Reset

Formula used

The Peclet number compares advective transport to diffusive transport.

  • Pe = U·L/α for heat transfer, where α is thermal diffusivity.
  • Pe = U·L/D for mass transfer, where D is mass diffusivity.
  • Pe = Re·Pr (heat) and Pe = Re·Sc (mass) when using dimensionless groups.
All calculations are performed in SI internally.

How to use this calculator

  1. Select Heat or Mass mode.
  2. Choose Direct or Reynolds-group method.
  3. Enter velocity U and characteristic length L with units.
  4. Provide α (or k, ρ, cp) for heat, or D for mass.
  5. Click Calculate, then export CSV or PDF if needed.

Example data table

Case Mode U (m/s) L (m) Diffusivity (m²/s) Pe Typical interpretation
1 Heat 0.20 0.05 α = 1.4×10⁻⁷ 7.14×10⁴ Advection dominates
2 Heat 0.005 0.01 α = 1.4×10⁻⁷ 357 Advection-leaning mixed
3 Mass 0.01 0.01 D = 2.0×10⁻⁹ 5.0×10⁴ Advection dominates
4 Mass 1.0×10⁻⁴ 0.001 D = 2.0×10⁻⁹ 50 Mixed transport
Examples are illustrative and depend on conditions.

Technical article

1) What the Peclet number measures

The Peclet number, Pe, compares bulk advection with diffusion. Small Pe means diffusion rapidly smooths temperature or concentration gradients. Large Pe means flow transports features downstream faster than diffusion can erase them, creating sharper boundary layers and stronger spatial nonuniformity.

2) Heat and mass forms used in this calculator

For heat transfer, Pe = U·L/α, with α as thermal diffusivity. For species transport, Pe = U·L/D, with D as mass diffusivity. Both are dimensionless, so the result depends on choosing U and L that represent your actual transport path and gradient scale.

3) Choosing a defensible characteristic length

Because Pe scales linearly with L, pick it carefully. In pipes, L is commonly diameter or hydraulic diameter. Over plates or cylinders, L may be body length or diameter. In porous media, grain size or pore length is often used. Select the distance across which diffusion must act to relax gradients.

4) Diffusivity data and typical magnitudes

Water near room temperature has α ≈ 1.4×10⁻⁷ m²/s, while air is roughly 2×10⁻⁵ m²/s. Molecular mass diffusivities are often 10⁻⁹ to 10⁻¹⁰ m²/s in liquids and near 10⁻⁵ m²/s in gases. Property realism is as important as geometry.

5) Regime hints from Pe values

Pe ≪ 1 suggests diffusion-dominated behavior; Pe ≫ 1 suggests advection-dominated behavior. Many systems fall between these extremes. Microchannels can have moderate Pe because L is small, even at noticeable velocities. Large ducts, rivers, and atmospheric flows often produce very large Pe values.

6) Connection to Re, Pr, and Sc

This tool can also compute Pe from Pe = Re·Pr (heat) or Pe = Re·Sc (mass). For example, water around 20°C has Pr ≈ 7, so Re = 10,000 implies Pe ≈ 70,000. For dilute solutes in water, Sc commonly ranges from hundreds to thousands.

7) Practical design implications

High Pe implies thin thermal or concentration boundary layers, strong axial transport, and increased sensitivity to entrance effects or poor mixing. Low Pe supports lumped models and faster cross-domain equilibration. In design, Pe helps decide whether you must resolve diffusion in simulations or can prioritize convection-dominated numerics.

8) Reporting and common pitfalls

Report U, L, diffusivity source, and units with Pe. Unit mistakes are common: converting cm²/s to m²/s multiplies by 10⁻⁴. Ensure α, D, ρ, μ, c_p, and k are positive. When using Re·Pr or Re·Sc, verify Re and Pr/Sc were computed from consistent properties.

FAQs

1) What is a typical Peclet number for water in a small pipe?

With U = 0.2 m/s, L = 0.05 m, and α = 1.4×10⁻⁷ m²/s, Pe ≈ 7.1×10⁴. That usually indicates advection-dominated heat transport and thin thermal boundary layers.

2) Should I use diameter or length for L in a tube?

Use the scale that matches the dominant gradient. For radial diffusion across the pipe, diameter is common. For axial diffusion along the flow, a streamwise length may be more appropriate.

3) Why does the calculator offer Pe = Re·Pr or Pe = Re·Sc?

In many correlations, Re and Pr or Sc are already known or tabulated. Using their product provides Pe consistently, and it helps connect transport behavior to flow regime and material properties.

4) How do I estimate thermal diffusivity if I do not know α?

You can compute α from α = k/(ρ c_p). Enter thermal conductivity, density, and specific heat using consistent units. The calculator converts to SI internally before computing α.

5) What does Pe near 1 mean physically?

Pe ≈ 1 means advection and diffusion contribute comparably. You should expect neither mechanism to dominate, so models or simulations should represent both accurately.

6) Why is my Peclet number extremely large?

Large U, large L, or very small diffusivity will increase Pe. Double-check units, especially cm²/s versus m²/s, and confirm L matches your physical gradient length rather than total device size.

7) Can Peclet number be negative?

Pe is typically reported as a magnitude. A negative value usually comes from a sign convention in velocity or coordinate choice. Use absolute velocity for transport strength, and document the convention if direction matters.

Use Peclet insights to refine models and experiments confidently.

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