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Atlas / Physics / The Flow Thread

Field · Emerged 1883 – 1991

Turbulence

When a flow becomes irregular at every scale at once, what about it is still predictable?

4 chapters6 min read6 turning points1 open problem

Branched from
Fluid Dynamics + Statistical Mechanics
Branched into
Geophysical Fluid Dynamics
Figures
Osborne Reynolds, Lewis Fry Richardson, Geoffrey Ingram Taylor, Andrey Kolmogorov, Lev Landau, Steven Orszag, Parviz Moin, John Kim

In brief

Above a certain speed, smooth flow stops being possible. Osborne Reynolds showed this in 1883 by injecting dye into water in a glass pipe: below a threshold the filament of dye ran straight down the tube, above it the dye burst into eddies and filled the pipe. Nothing about the fluid had changed. What changed was the balance between inertia and viscosity, and past the threshold the equations' solutions are no longer steady, no longer symmetric, and no longer repeatable in detail.

Turbulence was therefore approached the way thermodynamics approached a gas: give up on the individual motions and look for laws obeyed by the statistics. The results are remarkable for a subject with no solution. Lewis Fry Richardson's picture of energy passing from large eddies to smaller ones, and Andrey Kolmogorov's dimensional argument from it in 1941, predict that the energy in a turbulent flow is distributed across scales according to a power law with exponent −5/3-5/3, independent of what is being stirred, how, or with what fluid. That prediction has been confirmed in the ocean, the atmosphere, wind tunnels and liquid helium. It is also known to be not quite right, and the corrections have resisted eighty years of work.

Key ideas

Transition to turbulenceEnters 1883

Above a critical Reynolds number, laminar flow is unstable: small disturbances grow instead of decaying. The critical value depends on the geometry and on how clean the inlet is — about 2,000 for a pipe in practice, and far higher if disturbances are carefully suppressed.

Energy cascadeEnters 1922

Energy is fed in at large scales by whatever stirs the flow, passed down through eddies of decreasing size by the nonlinear term, and finally converted to heat by viscosity at the smallest scales. In between, energy is neither created nor destroyed, only handed on.

Statistical descriptionEnters 1935 – 1938

Since individual realisations are irreproducible, the objects of study are averages: correlations between velocities at two points, structure functions of velocity differences, and the distribution of energy across scales.

The five-thirds lawEnters 1941

In the range of scales between stirring and dissipation, the energy spectrum is E(k)=C ε2/3k−5/3E(k) = C\,\varepsilon^{2/3}k^{-5/3}, where ε\varepsilon is the rate of energy dissipation per unit mass. It follows from dimensional analysis alone, given the assumption that only ε\varepsilon matters.

Dissipation scaleEnters 1941

The size at which viscosity finally wins, η=(ν3/ε)1/4\eta = (\nu^{3}/\varepsilon)^{1/4}. The ratio of the largest scale to this one grows as Re3/4\mathrm{Re}^{3/4}, which is why simulating a high-Reynolds-number flow is so expensive.

IntermittencyEnters 1944 – 1962

Violent events — thin sheets and tubes of intense vorticity — are far more common than a Gaussian description allows, so the dissipation is not spread evenly. This is why the scaling exponents deviate from Kolmogorov's values, increasingly at higher orders.

Chapter I

When Smooth Flow Stops Being Available

Osborne Reynolds built an apparatus of great simplicity: a glass pipe, a tank of still water, and a fine nozzle introducing dye at the entrance. At low flow rates the dye travelled the whole length of the pipe as a straight thread. Open the valve further and at some point the thread wavered, then broke into eddies that mixed through the entire cross-section within a few diameters.

The transition happened at a fixed value of UD/νUD/\nu, whatever the pipe diameter and whatever the liquid. It was also sensitive to how disturbed the inlet was: with care, laminar flow could be maintained to much higher speeds. Both facts point the same way. Turbulence is not a property of the fluid but a question about the stability of a solution — above a critical Reynolds number the smooth flow still satisfies the equations, and no longer survives being nudged.

What takes its place is a flow that is irregular in space, unsteady in time, sensitive to initial conditions and not reproducible in detail. Two runs of the same experiment give different velocity records. This is a problem not of measurement but of what to even ask for. The response, over the following fifty years, was to stop asking about the flow and ask about its statistics — the same move statistical mechanics made when it stopped tracking molecules.

Chapter II

The Cascade

Lewis Fry Richardson supplied the physical picture in 1922, in a book otherwise devoted to forecasting weather by hand:

Big whirls have little whirls that feed on their velocity, and little whirls have lesser whirls and so on to viscosity.

Energy enters at the scale of whatever stirs the flow — the pipe diameter, the aircraft, the width of the ocean current. Viscosity can only remove energy where velocity gradients are steep, which means at very small scales. The nonlinear term does the transport in between, breaking large motions into smaller ones. In the middle of that range, energy is neither added nor dissipated; it merely passes through at a rate ε\varepsilon.

G. I. Taylor made the statistics precise in 1935, defining turbulence by the correlation between velocities at two points and introducing homogeneous isotropic turbulence — an idealisation that no real flow satisfies and in which nearly all theory is still done.

Then Andrey Kolmogorov, in two short papers in 1941, extracted quantitative predictions from the cascade picture with almost no mathematics.

Chapter III

A Closer Look: Two Paragraphs, Three Predictions, and the Cost of Checking Them

Kolmogorov's hypothesis is a statement about what the middle of the cascade can depend on. At separations rr much smaller than the stirring scale LL and much larger than wherever viscosity acts, the flow has forgotten how it was stirred and does not yet feel viscosity. The only quantity available is ε\varepsilon, the energy flux per unit mass, with dimensions

[ε]=energymass×time=m2s3.[\varepsilon] = \frac{\text{energy}}{\text{mass} \times \text{time}} = \frac{\mathrm{m^{2}}}{\mathrm{s^{3}}}.

Prediction one. The typical velocity difference δu\delta u across a separation rr can only be built from ε\varepsilon and rr. The only combination with units of velocity is

δu∼(εr)1/3.\delta u \sim (\varepsilon r)^{1/3}.

Prediction two. The energy per unit wavenumber E(k)E(k) has units of m³/s². Built from ε\varepsilon and kk (units 1/m), the only possibility is

E(k)=C ε2/3k−5/3.E(k) = C\,\varepsilon^{2/3} k^{-5/3}.

This is the five-thirds law, and C≈1.5C \approx 1.5 turns out to be very nearly the same in every flow measured.

Prediction three. Viscosity takes over where the local Reynolds number falls to one. With ν\nu (units m²/s) now allowed, the only length is

η=(ν3ε)1/4.\eta = \left(\frac{\nu^{3}}{\varepsilon}\right)^{1/4}.

Now put numbers on the last one, because it is the reason turbulence remains computationally out of reach. Estimate ε∼U3/L\varepsilon \sim U^{3}/L, as the cascade picture requires, and the ratio of the largest to the smallest scale becomes

Lη=(L4U3ν3L)1/4=Re3/4.\frac{L}{\eta} = \left(\frac{L^{4}U^{3}}{\nu^{3}L}\right)^{1/4} = \mathrm{Re}^{3/4}.

A simulation that resolves every scale needs a grid spacing of order η\eta across a box of size LL, in three dimensions, so the number of grid points is

N∼(Re3/4)3=Re9/4.N \sim \left(\mathrm{Re}^{3/4}\right)^{3} = \mathrm{Re}^{9/4}.

For an aircraft wing at Re=107\mathrm{Re} = 10^{7}:

N∼(107)9/4=1015.75≈5.6×1015 points.N \sim \left(10^{7}\right)^{9/4} = 10^{15.75} \approx 5.6\times10^{15} \text{ points}.

Storing five numbers per point in double precision is

5.6×1015×5×8 bytes≈2.2×1017 bytes=220 petabytes,5.6\times10^{15} \times 5 \times 8 \text{ bytes} \approx 2.2\times10^{17} \text{ bytes} = 220 \text{ petabytes},

which is more memory than exists in any machine. The time step must also shrink with the grid, adding a further factor of about Re3/4≈2×105\mathrm{Re}^{3/4} \approx 2\times10^{5} steps per flow-through time, bringing the operation count for a single flow-through to the order of 102110^{21}. On a machine doing 101810^{18} operations per second — exascale, achieved in 2022 — that is around a thousand seconds of computing per flow-through time, if memory were free and the efficiency perfect. Neither holds.

This is why engineering does not simulate turbulence directly, and why the closure problem is not a theoretical nicety. Every aircraft, engine and weather forecast computes a modelled turbulence whose coefficients were fitted to experiments, and the exponent 9/49/4 says that no foreseeable computer changes that.

Chapter IV

Where K41 Is Wrong

Lev Landau objected almost immediately, at a seminar, and the objection is subtle. Kolmogorov treats ε\varepsilon as a constant. It is not: dissipation fluctuates violently in space and time, concentrated in thin sheets and filaments of intense vorticity with relatively quiet fluid between them. Averaging ε2/3\varepsilon^{2/3} is not the same as taking the two-thirds power of the average, so the predictions should be corrected — and the corrections should grow with the order of the statistic being measured.

Measurements confirm this. The five-thirds law for the energy spectrum, a second-order quantity, holds beautifully. Higher-order structure functions deviate systematically from the 1941 exponents, by amounts that increase with order, and the pattern is reproducible across very different flows. Kolmogorov published a refined theory in 1962 assuming a lognormal distribution of local dissipation; it is known to be internally inconsistent at high orders. Multifractal models describe the data without deriving it.

So the position after eighty years is this. A dimensional argument whose central assumption is demonstrably false makes a prediction that is right to within a percent or two, and the corrections to the false assumption have not been derived from the equations by anyone. The deviations are small, universal-looking, and unexplained — a combination that keeps the problem alive.

What turbulence looks like in a rotating, stratified fluid the size of a planet, where the cascade runs partly backwards and large structures organise themselves out of small ones, is the subject of geophysical fluid dynamics.

Applications

Where it is used

  • Engineering

    Mixing, drag and heat transfer

    Turbulence is a nuisance in a pipeline, where it multiplies the pumping power required, and indispensable in a combustion chamber, where it mixes fuel and air thousands of times faster than diffusion would. Heat exchangers are designed to promote it; aircraft wings are designed to delay it on the forward part of the surface and then trip it deliberately, because a turbulent boundary layer separates later than a laminar one and the drag penalty is smaller than the wake.

    › Sources (1)
    • Pope, S. B. (2000). Turbulent Flows. Cambridge University Press.
  • Ecology↗ Biology · Community Ecology

    Finding food in a turbulent ocean

    Chemical signals in water do not spread as smooth gradients; turbulence tears them into thin filaments separated by clean water, so a crab or a copepod tracking a scent receives intermittent bursts rather than a rising concentration. Search strategies in marine animals make sense only against this statistical structure, and the same applies to insects following odour plumes in air.

    › Sources (2)
    • Weissburg, M. J. (2000). The fluid dynamical context of chemosensory behavior. Biological Bulletin 198: 188–202.
    • Celani, A., Villermaux, E. & Vergassola, M. (2014). Odor landscapes in turbulent environments. Physical Review X 4: 041015.
  • Scaling arguments↗ Mathematics · Differential Equations

    A power law from dimensions alone

    Kolmogorov's derivation is the standard example of what dimensional analysis can do when the list of relevant quantities is right, and of how much rests on that list. It is taught across applied mathematics as a model for intermediate asymptotics: identify the range where the boundaries have been forgotten and the cut-off is not yet felt, and the answer is forced.

    › Sources (1)
    • Barenblatt, G. I. (1996). Scaling, Self-Similarity, and Intermediate Asymptotics. Cambridge University Press.

Open problems

Where the map runs out

Open

Closing the equations for the averages

Open as of 2026; every model in engineering use contains coefficients fitted to experiment.

Averaging the Navier–Stokes equations produces an equation for the mean velocity that contains a new unknown, the correlation of the fluctuations. Writing an equation for that introduces a third-order correlation, and so on without end. No way has been found to close the hierarchy from the equations themselves, so every practical calculation inserts a model — a mixing length, an eddy viscosity, a two-equation scheme — whose constants are measured rather than derived.

Why it is hard

The nonlinear term couples all scales, so the small-scale motions that are being modelled depend on the large-scale ones being computed. Nothing in the problem separates cleanly, and the quantity to be modelled is not small compared with the one being solved for. The anomalous scaling exponents that intermittency produces have not been derived either, which means even the statistics of the inertial range are not fully understood.

What resolving it unlocks

Aircraft, engines, reactors, pipelines and climate models all compute turbulent flows with fitted models, and the models fail in regimes they were not fitted for. A derivation would replace calibration with prediction in a large part of engineering.

› Sources (2)
  • Pope, S. B. (2000). Turbulent Flows. Cambridge University Press, chapters 10–13.
  • Sreenivasan, K. R. (1999). Fluid turbulence. Reviews of Modern Physics 71: S383–S395.

Further reading

  1. Frisch, U. (1995). Turbulence: The Legacy of A. N. Kolmogorov. Cambridge University Press.

    The clearest account of the cascade, K41 and what intermittency does to it.

  2. Davidson, P. A. (2015). Turbulence: An Introduction for Scientists and Engineers, 2nd edition. Oxford University Press.

    A readable graduate text that keeps the physical picture in front of the formalism.

  3. Pope, S. B. (2000). Turbulent Flows. Cambridge University Press.

    The reference for the modelling side, honest about where the constants come from.