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Reynolds Number

Reynolds number calculation, flow regime classification, and engineering applications.

reynoldsnumber

Overview

The Reynolds number is a dimensionless quantity that expresses the ratio of inertial forces to viscous forces within a fluid. It is the primary parameter for predicting whether flow through a pipe, duct, or around a body is laminar, transitional, or turbulent.

For internal flow the characteristic length is the hydraulic diameter DhD_h, which equals the pipe inner diameter for circular cross-sections.

Key Formulas

Reynolds Number (SI)

Re=ρvDμRe = \frac{\rho \, v \, D}{\mu}

Equivalently, using kinematic viscosity ν=μ/ρ\nu = \mu / \rho:

Re=vDνRe = \frac{v \, D}{\nu}

Reynolds Number (Imperial — pipe flow)

Re=7745.8  u  dhνRe = 7745.8 \;\frac{u \; d_h}{\nu}

where uu is in ft/s, dhd_h is in inches, and ν\nu is in centistokes (cSt).

Variables

8 rows
Symbols and units used in Reynolds number calculations
Symbol
Description
Unit
ReReynolds number
ρFluid densitykg/m³
vMean flow velocitym/s
DCharacteristic length (hydraulic diameter)m
μDynamic viscosityPa·s
νKinematic viscosity (μ / ρ)m²/s
uFlow velocity (Imperial)ft/s
d_hHydraulic diameter (Imperial)in

Source: engineeringtoolbox.com

Flow Regimes

3 rows
Flow regime classification for internal pipe flow
Flow Regime
Reynolds Number Range
Typical Context
LaminarRe < 2300Highly viscous fluids; low velocities
Transitional2300 ≤ Re ≤ 4000Unstable; depends on surface roughness
TurbulentRe > 4000Most industrial pipe flows

Source: engineeringtoolbox.com

Calculator

Reynolds Number (SI)

Reynolds Number from Kinematic Viscosity

Unit Converter

Reynolds Number Unit Converter

Schedule 40 Water Flow Chart

The source chart for water flow in Schedule 40 steel pipe is represented below as an interactive calculated chart. Values use water at approximately 20 °C with kinematic viscosity 1.004 cSt and typical Schedule 40 internal diameters.

Reynolds Number for Water Flow in Schedule 40 Steel Pipe

Example Calculation

Given: A fluid with specific gravity 0.91 and dynamic viscosity 0.38 Pa·s flows at 2.6 m/s through a 25 mm diameter pipe.

  1. Density: ρ=0.91×1000=910  kg/m3\rho = 0.91 \times 1000 = 910 \;\text{kg/m}^3
  2. Reynolds number:

Re=910×2.6×0.0250.38156Re = \frac{910 \times 2.6 \times 0.025}{0.38} \approx 156

Since Re1562300Re \approx 156 \ll 2300, the flow is clearly laminar.

Restored Original Source Tables

The following tables are restored from the original source page to preserve the complete reference data. The cached source tables outside the engineering chart are shared search/layout artifacts, not Reynolds-number data tables, and are intentionally not copied as reference data.

The source page references a Reynolds Number Calculator App for offline mobile use. The calculators above preserve the same core calculations directly in the page.

Original Source Images

The following original source images are preserved to avoid losing visual reference material. When an image contains chart or tabular data, its extracted values are represented in the page tables, calculators, or interactive charts; remaining images are retained as visual source references.

Reynolds number chart water flow schedule 40 steel pipe

Engineering Notes

  • Turbulent flow is the norm in most water, air, and process piping systems. Laminar conditions are typically limited to heavy oils, polymer melts, or very small-diameter / low-velocity flows.
  • The transitional range (2300–4000) is sensitive to entrance conditions, pipe roughness, and vibration. Design conservatively by assuming turbulent behaviour above Re ≈ 2300.
  • For non-circular ducts always use the hydraulic diameter Dh=4A/PD_h = 4A / P, where AA is the flow area and PP is the wetted perimeter.
  • The Imperial shortcut (Re=7745.8  u  dh/νRe = 7745.8 \; u \; d_h / \nu) embeds the unit conversion from inches and centistokes. Verify that viscosity is given in cSt before applying it.
  • The Reynolds number also governs external flows (around cylinders, spheres, airfoils) but the critical Re values for transition differ from the pipe-flow thresholds listed above.

References