phenomenon

turbulent mixing

Turbulence causes efficient mixing and energy transfer in fluids, often unpredictably.
42 related articles · 6 formulas

Description

Turbulent mixing is the process by which turbulence—chaotic, swirling fluid motion—dramatically accelerates the blending of different quantities like heat, momentum, or chemical species. In a calm fluid, mixing relies on slow molecular diffusion; turbulence creates eddies that stretch and fold fluid parcels, exponentially increasing the surface area over which diffusion acts. This makes turbulent mixing vastly more efficient than laminar mixing, which is why stirring cream into coffee works so well and why pollutants spread so quickly in the atmosphere.

History

The concept of turbulent mixing has roots in the work of Lewis Fry Richardson, who in the 1920s described the energy cascade in turbulence with his famous rhyme about big whorls having little whorls. The statistical theory of turbulent mixing was later developed by Andrey Kolmogorov in 1941.

How it works

Turbulence consists of a cascade of eddies of many sizes. Large eddies, energized by the flow's overall motion, break into smaller eddies, transferring energy down to scales where viscosity dissipates it as heat. During this cascade, fluid parcels are continuously stretched and folded, like a baker kneading dough. This stretching creates thin filaments and sheets, so that adjacent fluid layers come into intimate contact over enormous areas, allowing molecular diffusion to homogenize the mixture rapidly.

In practice

Turbulent mixing is central to combustion in engines, chemical reactors, atmospheric pollutant dispersion, and ocean heat transport. It also plays a role in astrophysical processes like planet formation in gas disks.

Fun fact

In quantum fluids, turbulent mixing can occur in a superfluid state where vortices are quantized, and the mixing dynamics differ fundamentally from classical fluids, as explored in simulations on superconducting chips.

Concept graph →

Formulas

$$\dot{\rho}_1 + 3H(\rho_1 + p_1) = Q, \quad \dot{\rho}_2 + 3H(\rho_2 + p_2) = -Q$$
Energy exchange between two cosmic fluids preserves total energy.
What is in the formula
ρ_1variableEnergy density of fluid 1 — energy density joule per cubic metre
ρ_2variableEnergy density of fluid 2 — energy density joule per cubic metre
p_1variablePressure of fluid 1 — pressure pascal
p_2variablePressure of fluid 2 — pressure pascal
HvariableHubble parameter — hubble parameter per second
QvariableEnergy transfer rate between fluids — energy transfer rate joule per cubic metre per second
˙operatorDerivative with respect to cosmic time — time derivative
\dot{ρ}_{{dm}}+3hρ_{{dm}}=q,\quad\dot{ρ}_{{de}}+3h(ρ_{{de}}+p_{{de}})=-q · 2607.04460
$$Q = \frac{E_{\text{fusion}}}{E_{\text{loss}}}$$
Ratio of fusion energy produced to energy input.
What is in the formula
E_fusionvariableenergy produced by fusion reactions — energy joule
E_lossvariableenergy lost from the system — energy joule
q=\frac{e_{fusion}}{e_{loss}} · 2601.09458
$$\Phi_{\text{eff}} \geq \Phi_{\text{min}}$$
Effective flux must exceed a minimum threshold value.
What is in the formula
Φ_effvariableeffective flux — flux weber
Φ_minvariableminimum threshold flux — flux weber
\phi_{{eff}}=\phi_{{int}}t_{{net}}\geq\phi_{{bel,min}} · 2607.01479v1
$$v_{\rm term} \propto \dot{m}^{-1/2}$$
Terminal outflow velocity scales with accretion rate.
What is in the formula
v_{\rm term}variableTerminal outflow velocity — velocity metre per second
\dot{m}variableMass accretion rate — mass accretion rate kilogram per second
v_{\rmterm}=7.46*10^2(\dot{m}_3/2)^{-1/2}{\rmkms^{-1}} · 2607.17448v1
$$\alpha \Delta T = \eta \dot{\gamma}^2$$
Temperature rise from viscous heating balances dissipation rate.
What is in the formula
αvariablethermal expansion coefficient (or a thermal response coefficient) — thermal expansion coefficient per kelvin
ΔTvariabletemperature rise — temperature difference kelvin
ηvariableviscosity (dynamic viscosity) — dynamic viscosity pascal second
γ̇variableshear rate (strain rate) — shear rate per second
α(t_e-t_{{ph}})=m\eta_{xx}(\frac{dv}{dy})^2 · 2606.27788
$$\frac{d}{dy} \left( \eta \frac{dV}{dy} \right) = -\frac{F}{\rho}$$
Shear stress gradient balances body force in fluid flow.
What is in the formula
yvariablespatial coordinate perpendicular to flow — position metre
Vvariablefluid velocity in the flow direction — velocity metre per second
Fvariablebody force per unit volume acting on the fluid — force density newton per cubic metre
ρvariablefluid mass density — mass density kilogram per cubic metre
ηconstantdynamic viscosity of the fluid — dynamic viscosity = material-dependent pascal second
d/dyoperatorderivative with respect to y — ordinary derivative
\frac{d}{dy}(\eta_{xx}^{{nl}}\frac{dv}{dy})=-\frac{ee}{m} · 2606.27788

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