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Reynolds Number: Laminar to Turbulent

Reynolds' dye experiment, run frame by frame — a straight thread that starts to wobble and then vanishes into the flow.

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The Reynolds number is the ratio of inertial to viscous forces, Re = ρvD/μ, and it decides whether disturbances in a flow are amplified into turbulence or damped back into orderly layers — a dimensionless number, so the same value means the same behaviour in a capillary and in an oil pipeline.

Reynolds' dye experiment

In 1883 Osborne Reynolds injected a thread of dye into water flowing through a glass pipe and slowly opened the valve. The historical setup is still the clearest demonstration of the idea.

  1. 1At low flow the dye stays a sharp straight line the length of the tube — laminar flow, in parallel layers that do not mix.
  2. 2Open further and the thread begins to oscillate without breaking up — transitional, with disturbances no longer being damped.
  3. 3Open fully and the dye disperses within a pipe diameter — turbulent, with chaotic eddies carrying fluid across the flow.

In laminar flow, mixing across the pipe happens only by molecular diffusion — far too slow to blur the thread. Turbulent mixing is thousands of times faster.

The ratio

Reynolds' insight was that no single variable decides this — a ratio does. Inertial forces carry a disturbance onward and amplify it; viscous forces smear it out and kill it.

Re = ρvD/μ = vD/ν. High Re means inertia wins and disturbances grow. Low Re means viscosity wins and they are damped. Because it is dimensionless, all the units cancel and the number travels between scales.

The thresholds, and how far they travel

GeometryLength scale in ReTransition at roughly
Circular pipeDiameter D2300 laminar → 4000 turbulent
Flat plateDistance x from the leading edge5 × 10⁵
Sphere or cylinderDiameter D2 × 10⁵ (the drag crisis)
Open channelHydraulic radius R≈ 500

The number 2300 belongs to pipes. Quoting a Reynolds number without saying which length scale it uses is meaningless — and the thresholds do not carry between geometries.

Transition is genuinely a range rather than a line. With an exceptionally smooth inlet and no vibration, laminar pipe flow has been sustained to Re well past 10⁵ in the laboratory. It is a metastable state; a real pipe with real disturbances does not achieve it.

Two regimes, two velocity profiles

LaminarTurbulent
ProfileExactly parabolicBlunt, flattened core
Centre velocity2 × mean≈ 1.2 × mean
Wall gradientGentleSteep — the whole change is near the wall
Friction factorf = 64/Re, derivableFrom the Moody chart, measured
Head loss goes asv≈ v²
MixingMolecular diffusion onlyCross-stream eddies, orders of magnitude faster

The flatter turbulent profile looks gentler and is not. Flattening the core pushes the entire velocity change into a thin layer at the wall, so the shear there — and the friction — is much higher.

Choosing a regime

Turbulence is not a failure mode. Which regime you want depends entirely on what the flow is for.

  • Want laminar: long pipelines, lubrication films, microfluidics, blood flow. Low friction, low pumping cost, predictable.
  • Want turbulent: heat exchangers, combustors, mixers, chemical reactors. The cross-stream transport is the entire point.

And because Re is dimensionless, matching it between a model and the full-scale thing makes the two flows behave alike. That is the foundation of towing-tank and wind-tunnel testing, and it is the most-used instance of dimensional analysis in engineering.

The numbers you will be asked for

Reynolds number

Re = ρvD / μ = vD / ν

Pipe thresholds

Re < 2300 laminar · Re > 4000 turbulent

Laminar friction factor

f = 64 / Re

derivable, no chart needed

Hydraulic diameter

D_h = 4A / P

for non-circular ducts

Model similarity

Re_model = Re_full

match it and the flows correspond

Watch it work

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Check yourself

question 1 / 4

One question at a time. Pick an answer to see why it is right or wrong, then move on — there is no score to keep and nothing is saved.

What is the Reynolds number comparing?
You compute Re = 3000 for a flat plate. What does that tell you?
Turbulent flow has a flatter velocity profile. Why does that mean more friction, not less?
A heat exchanger is deliberately designed to run turbulent. Why?

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4 still unanswered — the dots above jump straight to them.