01

THE INTUITION

Follow the water — drop dye into a smooth, viscous flow and watch it fade.

LIVE SIMULATIONSIM/01 · 2D TRACERS
PEAK SPEED 100% OF INITIAL · t = 0.0
INTERNAL FRICTION ν0.08
LESS SMOOTHINGMORE SMOOTHING
TIME0%
STARTLATE

Watch one dot. It circles its cell as the flow slows. Longer arrows mean faster motion. Drag the time slider to scrub; press play to let the fluid run.

02

THE PROBLEM

Does friction always win?

LIVE SIMULATIONSIM/02 · STRETCH vs SMOOTH
CORE SPEED 1.00× · CORE WIDTH 100%
STRETCHING RATE1.00
NONEVIOLENT
FRICTION ν1.00
THINSYRUP

A toy race, not the equations. A vortex tube is stretched along its axis (narrower, faster) while friction widens and slows it. Tilt the two knobs and watch which side wins: a bounded plateau, or a run toward the top.

03

THE CONSTRUCTION

A shrinking core. A rising speed.

LIVE SIMULATIONSIM/03 · 3D SCHEMATIC · DRAG TO LOOK
AXIAL STRETCHING ↑ · INWARD SPIRAL · 0% TOWARD SINGULAR TIME
TOWARD THE SINGULAR TIME0%
EARLYτ = 10⁻⁶

Not a numerical solution. Dashed circles mark the initial core size. The progression approaches the deadline logarithmically and stops at τ = 10⁻⁶. Strand colours identify strands, not speeds.

04

THE KEY DISTINCTION

Faster flow. Less core energy.

LIVE READOUTSIM/04 · SCALING LAWS
SPEED (LOG) vs CORE ENERGY (LINEAR)
CORE SPEEDINITIAL SPEED = 1×
CORE ENERGY100.0%INITIAL ENERGY = 100%
TIME REMAINING τ1.0e+0
EARLIERCLOSER TO THE SINGULAR TIME

Illustrative ratios. Speed is on a log scale and energy on a linear one. The percentages measure progress through this illustration, not elapsed physical time.

05

THE REPORTED RESULT

A counterexample — not a formula for every fluid.

LIVE SIMULATIONSIM/05 · PEAK SPEED TRACE
|u|max AGAINST TIME · FORCED FROM REST

Two traces. With forcing off, a fluid at rest stays at rest and a stirred one decays — bounded forever. With forcing on, the trace follows the reported scaling and climbs off the chart as tT. Illustrative curves, not the paper's data.

06

READ THE EQUATION

Changing motion, carried motion, pressure, friction, and an outside push — all in balance.

TERM EXPLORERSELECT A TERM TO READ IT IN WORDS

Select a term above.

And one more line: ∇ · u = 0 — incompressibility. A moving parcel of fluid keeps its volume; squeeze it one way and it must expand another. It is what turns pressure into a constraint rather than a free variable.

◈ BEHIND THE VISUALS

SIM/01 integrates tracers through the exact Taylor–Green field u = sin x cos y e−2νt, v = −cos x sin y e−2νt, with pressure p = ¼(cos 2x + cos 2y) e−4νt, on a periodic domain, by fourth-order Runge–Kutta. This is a genuine solution of the equations and it never blows up.

SIM/02 is a two-variable toy — core width and core speed under a stretching term and a diffusion term — built to show a race, not to solve Navier–Stokes. SIM/03 is a drawn schematic: it exaggerates the change in proportions, uses independent bead timing, approaches the deadline logarithmically and stops at τ = 10⁻⁶. It shows central inflow and axial outflow and omits the full profile's asymmetry, the distant radial outflow and the correction terms.

SIM/04 and SIM/05 plot the paper's stated scaling bounds U ≍ τ−1/2−h and Ecore ≍ τ1/2−3h with h = 0.005 and unit constants, as an illustration and not the exact solution. Strand colours are decorative and do not reproduce any measured data.