Turbulence & the Reynolds Number
Osborne Reynolds discovered in 1883 that a single dimensionless parameter — the ratio of inertial to viscous forces — predicts whether a flow will be smooth and orderly or chaotic and turbulent. Despite over a century of research, turbulence remains one of the last unsolved problems of classical physics. Yet engineers harness empirical models to design aircraft, pipelines and weather systems every day.
1. The Reynolds Number
The Reynolds number Re compares the magnitude of inertial forces (which promote turbulence) to viscous forces (which suppress it):
2. Laminar–Turbulent Transition
In his 1883 dye-stream experiment, Reynolds injected coloured water into a glass pipe and varied the flow rate. Below a critical Re the dye flowed in a smooth thread; above it the dye mixed chaotically throughout the cross-section.
Transition is not a sharp threshold — it depends on inlet disturbances, pipe roughness, and free-stream turbulence intensity. The Orr-Sommerfeld equation describes the linear stability: small perturbations grow when the eigenvalues of the associated operator have positive imaginary parts.
3. Kolmogorov Energy Cascade
In 1941 Kolmogorov proposed a statistical theory of fully developed turbulence. Energy is injected at large scales (integral scale L), cascades through a hierarchy of eddies, and dissipates as heat at the Kolmogorov microscale η:
4. Kármán Vortex Street
Flow past a bluff body (cylinder, bridge pier, chimney) sheds alternating vortices downstream at a characteristic frequency governed by the Strouhal number:
5. Boundary Layers
Near a solid surface the no-slip condition forces velocity to zero. The boundary layer thickness δ grows with distance x from the leading edge:
6. DNS, RANS and LES
DNS
Direct Numerical Simulation resolves all scales down to η. Exact but O(Re^(9/4)) cost. Used for Re ≤ 10 000 in research.
RANS
Reynolds-Averaged Navier-Stokes. Time-averages the equations, models all turbulence via a closure (k-ε, k-ω SST). Standard in industrial CFD.
LES
Large Eddy Simulation resolves large eddies directly, models only sub-grid scales (Smagorinsky model). 10–100× more expensive than RANS.
Hybrid RANS/LES
DES (Detached Eddy Simulation): RANS near walls, LES in free shear regions. Best balance of cost and accuracy for aerodynamics.
7. JavaScript Vortex Shedding Simulation
// 2D Kármán vortex street via point vortex method
class PointVortex {
constructor(x, y, gamma) {
this.x = x; this.y = y;
this.gamma = gamma; // circulation (+ = CCW, - = CW)
}
}
function inducedVelocity(vortices, px, py, core = 0.5) {
let u = 0, v = 0;
for (const vt of vortices) {
const dx = px - vt.x, dy = py - vt.y;
const r2 = dx*dx + dy*dy + core*core;
u += vt.gamma * dy / (2*Math.PI * r2);
v -= vt.gamma * dx / (2*Math.PI * r2);
}
return {u, v};
}
function stepVortices(vortices, U_inf, dt) {
const newPos = vortices.map(v => {
const others = vortices.filter(w => w !== v);
const {u, v: vel_v} = inducedVelocity(others, v.x, v.y);
return {x: v.x + (U_inf + u) * dt, y: v.y + vel_v * dt};
});
newPos.forEach((p, i) => { vortices[i].x = p.x; vortices[i].y = p.y; });
}
// Kármán street: shed vortices alternately above/below cylinder
const vortices = [];
let time = 0, shedTimer = 0;
const U = 1, D = 20, St = 0.2;
const shedPeriod = D / (St * U); // T = D/(St·U)
function shed(sign) {
const gamma = sign * 2 * Math.PI * U * D * 0.3;
vortices.push(new PointVortex(0, sign * D * 0.6, gamma));
}
function update(dt = 0.5) {
shedTimer += dt;
if (shedTimer >= shedPeriod / 2) {
shed(vortices.length % 2 === 0 ? 1 : -1);
shedTimer = 0;
}
stepVortices(vortices, U, dt);
time += dt;
// Remove vortices that have left the domain
while (vortices.length > 60) vortices.shift();
}
// Reynolds number monitor
function striationRe(U, D, nu = 1e-6) {
return U * D / nu;
}
8. Engineering Applications
- Aircraft design: Wing lift is critically affected by boundary-layer separation; turbulators and vortex generators delay stall by energising the boundary layer.
- Pipelines: Turbulent friction factor (Moody chart) determines pumping power requirements. Smooth pipes follow the Colebrook-White equation.
- Heat exchangers: Turbulence enhances convective heat transfer (Nusselt number Nu ∝ Re^0.8 × Pr^0.4 — Dittus-Boelter correlation).
- Wind engineering: Vortex-induced vibration governs the design of tall buildings, bridges, offshore platforms and power lines.
- Weather prediction: Atmospheric turbulence is the primary mechanism mixing momentum, water vapour and heat from the surface upward.