Flows and fields

A wall puts in exactly its own speed

A wall sliding in its own plane makes vorticity at a rate equal to its acceleration, with no viscosity in the rate. So however a wall is started, the vorticity it has put into the fluid is its speed, to the last digit; a wall that stops takes all of it back and leaves the fluid moving; and a spinning cylinder carries its whole circulation from the first instant, hidden behind an equal and opposite ring until viscosity carries the ring away.

Worth reading first: Where vorticity comes from · The wall that shakes.

Where vorticity comes from found that every scrap of vorticity in the flow past a body enters through its surface, and that the rate at which it enters contains no viscosity at all: evaluate the momentum equation on a stationary wall, where the velocity vanishes, and the diffusive flux of vorticity out of the wall is the pressure gradient along it. That essay ended by naming the wall it had left out — the one that moves.

The same four lines settle that one. Take a wall sliding in its own plane at a speed U(t)U(t) that it chooses, with the fluid stuck to it. On the wall the fluid’s velocity is the wall’s, so its acceleration there is dU/dtdU/dt, and the momentum equation evaluated at the surface keeps that one term:

dUdt=1ρpx+ν2uy2w.\frac{dU}{dt} = -\frac{1}{\rho}\frac{\partial p}{\partial x} + \nu\frac{\partial^2 u}{\partial y^2}\bigg|_{w}.

With ω=u/y\omega = -\partial u/\partial y, the last term is the diffusive flux of vorticity out of the wall, so

σ  =  νωyw  =  dUdt+1ρpx.\sigma \;=\; -\nu\frac{\partial\omega}{\partial y}\bigg|_{w} \;=\; \frac{dU}{dt} + \frac{1}{\rho}\frac{\partial p}{\partial x}.

A wall is a vorticity source whose strength is its own acceleration, added to the pressure term, and the viscosity has cancelled from the acceleration term for exactly the reason it cancelled from the pressure term. Everything below takes the pressure gradient to be zero and looks only at what acceleration does.

Three ways to reach the same speed leave three profiles with the same area. The vorticity above a wall in water brought to 0.1 m/s three ways — at once, by a steady ramp over 1 s, and by a smooth start over 1 s — 3 s after it began to move. The shapes differ: the wall started at once has the sharpest peak, 32.6 per second at the surface, and the ramps have spent part of their time making vorticity at a lower rate. The totals do not: 0.100000 and 0.100000 m/s for the two ramps, integrated across the computed profiles, and 0.1 m/s for the closed form. What a wall puts into a fluid by starting is its own speed, and how it started decides only where that vorticity is.
Fig. 1 The vorticity above a wall in water brought to 0.1 metres a second three ways — at once, by a steady ramp over a second, and by a smooth start over a second — three seconds after it began to move. The shapes differ: the wall started at once has the sharpest peak. The totals, integrated across the computed profiles, are 0.100000 metres a second for all three.

Three starts, one total

Integrate the source over time and the budget is immediate. The rate at which vorticity crosses the wall is dU/dtdU/dt, so the total that has crossed it by any instant is the wall’s speed at that instant, and nothing has left the fluid by any other route. A wall moving at 0.1 metres a second has put exactly 0.1 metres a second of vorticity, per unit of its area, into the fluid above it.

The figure shows what that does and does not fix. A wall started at once puts its whole budget in at the first instant, in a sheet of zero thickness that viscosity immediately begins to spread; three seconds later that vorticity has diffused a millimetre or two, with its peak still at the surface. A wall ramped up over a second has made its vorticity at a steady rate throughout that second, so some of it is three seconds old and some is two, and the profile is broader and lower. A smooth start differs again. The areas under the three curves are the same to six figures, because the area is the wall’s speed and all three walls are moving at the same speed.

That is a much stronger statement than it looks. The wall’s history is completely different in the three cases, and the viscosity could be anything: nothing about the total depends on either. The history decides where the vorticity is, and the viscosity decides how fast it spreads once it is there. How much of it there is was decided by the wall’s speed alone.

A calculation that knows only the flux

The source law was derived in two lines from an equation evaluated at a surface, and a derivation that short deserves a check that does not repeat it.

A solver told only that the wall's flux is its acceleration reproduces the no-slip wall. The vorticity above a wall in water started smoothly to 0.1 m/s over 1 s, at 0.5 s and 3 s, from two calculations. The lines come from solving for the velocity with the wall moving and no slip at it; the dots from solving for the vorticity alone, with no velocity anywhere in the calculation, a closed top, and the single statement that vorticity enters through the wall at a rate equal to the wall's acceleration. They differ by 8.1×10⁻⁷ and 8.2×10⁻⁷ of the peak. Across two wall histories and two viscosities a hundred times apart the worst disagreement is 1.0×10⁻³ of the peak, at the corners of the ramp. The source law is σ = dU/dt, and it holds with no viscosity in it.
Fig. 2 The vorticity above a wall in water started smoothly to 0.1 metres a second over a second, at half a second and at three, from two calculations. The lines solve for the velocity with the wall moving and no slip; the dots solve for the vorticity alone, told only that vorticity enters through the wall at a rate equal to the wall’s acceleration. They differ by less than a millionth of the peak.

The check is two calculations with nothing in common but the wall. The first solves for the velocity. It knows the wall’s speed at every instant and imposes no slip, the ordinary way, and its vorticity is read off afterwards as the slope of the velocity. The second solves for the vorticity directly, as a diffusing quantity in cells. It contains no velocity at all, it does not know the wall is moving, and its only information about the wall is a single number on the bottom face of the bottom cell: the flux dU/dtdU/dt.

If the source law were wrong — a factor of two, a missing term, a sign — the second calculation would put the wrong amount of vorticity in at the wrong rate, and the dots would drift off the lines. For a smooth start they agree to eight parts in ten million of the peak. Across two wall histories and two viscosities a hundred times apart the worst disagreement is a thousandth of the peak, and it sits at the corners of the steady ramp, where the acceleration jumps and a finite time step cannot follow it exactly.

The budget closes on the speed

The vorticity in the fluid is the wall's speed at every instant, however fast it got there. The total vorticity above a wall in water, per unit area, against time, for smooth starts to 0.1 m/s over 0.5 s, 1 s and 2 s, summed over the vorticity-only calculation — dots — against the wall's own speed, drawn as lines. The calculation contains no velocity: the only thing it knows about the wall is the rate at which vorticity crosses it. The largest difference between the summed vorticity and the wall's speed over all three runs is 3.3×10⁻⁷ m/s. The budget closes on the wall's speed, not on its history and not on the viscosity: a quick start makes vorticity fast and a slow one slowly, and both end with the same amount.
Fig. 3 The total vorticity above the wall, summed over the vorticity-only calculation, against time, for smooth starts over half a second, one second and two seconds, against the wall’s own speed drawn as lines. The largest difference over all three runs is a third of a millionth of a metre a second.

The same second calculation gives the budget directly. Its dots are the vorticity summed over every cell, and its lines are the wall’s speed. A fast start makes vorticity quickly and a slow one slowly, and at every instant of every run the sum sits on the speed.

That is Kelvin’s theorem arriving from the wall rather than from a material loop. Circulation is vorticity added up, and for this flow the circulation round a tall rectangle — up through the fluid far away, along the top where nothing moves, down, and back along the wall — is the wall’s speed times the rectangle’s length. The wall is the one side of that loop whose velocity changes, and the vorticity inside the loop changes to match it. Nothing is created in the interior; nothing is destroyed; it enters at the bottom, at the acceleration’s rate, and spreads.

What viscosity decides

If viscosity is absent from the amount, it must be present somewhere, and it is: in the distance.

Viscosity decides how far the vorticity has gone, and nothing about how much there is. How far the vorticity above a wall started at once has spread — the height of its centroid, 2√(νt/π) — against time, for water (ν = 1.0×10⁻⁶ m²/s), air (ν = 1.5×10⁻⁵ m²/s) and glycerol (ν = 1.0×10⁻³ m²/s), on logarithmic axes. The three lines are a thousandfold apart in viscosity and thirty-fold apart in height at every instant. Computed after one second, the centroids are 1.128 mm, 4.370 mm and 35.683 mm against 1.128, 4.370 and 35.682 in closed form, and the totals are 0.100000, 0.100000 and 0.100000 m/s. The same amount of vorticity, spread over layers whose thickness differs by thirty.
Fig. 4 How far the vorticity above a wall started at once has spread — the height of its centroid, 2√(νt/π) — against time, for water, air and glycerol, on logarithmic axes. The three are a thousandfold apart in viscosity and thirty-fold apart in height at every instant; after one second the computed centroids sit at 1.13, 4.37 and 35.7 millimetres. The totals are 0.100000 metres a second in every case.

A wall started at once under water, air and glycerol holds the same vorticity above it at every instant. After one second it is concentrated within about a millimetre of the surface in water, spread over four in air and over three and a half centimetres in glycerol, and the centroid of each moves out as the square root of the viscosity times the time — the diffusion length that the wall that shakes found for an oscillating wall and that sets how thick every boundary layer is.

So the division of labour is exact. The wall’s speed decides how much vorticity there is, and the viscosity decides where it is. A fluid with a thousand times less viscosity does not have less vorticity above a started wall; it has the same amount packed thirty times more tightly, with a peak thirty times higher — which is why the shear stress at a started wall, the peak vorticity times the viscosity, falls as the square root of the viscosity rather than as the viscosity itself.

A wall that stops

A wall that stops is a wall that accelerates the other way, and the source law applies unchanged.

A wall that stops takes back all its vorticity and none of the fluid's momentum. The vorticity above a wall in water started at once to 0.1 m/s and stopped at once after 1 s, at 1.5 s, 3 s and 8 s. Stopping is a second impulsive start in the other direction, so the wall injects an equal and opposite sheet of vorticity at its surface, and the profile carries both signs: the old vorticity diffused outwards, the new beneath it. The total, summed over the computed profiles, is zero to within 3.2×10⁻³⁰ m/s. The fluid's momentum per unit area is not zero: 0.0584, 0.0359 and 0.0206 mm·m/s, equal to the first moment of the vorticity to within 7.6×10⁻¹⁶ — falling from 0.1128 at the moment of stopping as the stopped wall drags the fluid back. Net vorticity says whether the wall is moving; the fluid's momentum is where that vorticity sits.
Fig. 5 The vorticity above a wall in water started at once to 0.1 metres a second and stopped at once a second later, at 1.5, 3 and 8 seconds. The stop injects an equal and opposite sheet of vorticity at the surface, so the profile carries both signs. The total is zero to within the rounding of the arithmetic; the fluid’s momentum is not, and equals the first moment of the vorticity to fifteen figures.

Stopping is an impulsive start in reverse, so it injects a sheet of vorticity equal and opposite to the one the start put in, at the surface, beneath the old vorticity that has had a second to diffuse outwards. From then on the two sheets spread together, and the profile has a positive layer above and a negative layer below. The total is zero, as it must be for a wall with no speed.

The fluid is still moving. Its momentum per unit area is 0.058 millimetre-metres per second half a second after the stop and 0.021 after seven seconds, falling because the stopped wall now holds the fluid back. And that momentum is exactly the first moment of the vorticity: integrating the velocity by parts gives udy=yωdy\int u\,dy = \int y\,\omega\,dy, so a profile whose vorticity sums to zero but whose positive part sits further from the wall than its negative part carries momentum.

That separates two things the word “vorticity” tends to run together. The net vorticity above a wall records whether the wall is moving now. The distribution of vorticity records what the fluid is doing, and a fluid can be in motion with no net vorticity above it at all. An oscillating wall is the extreme case: its net vorticity follows its velocity and averages to zero over a cycle, while the wave of alternating layers it sends upwards carries energy away into the fluid for as long as it shakes.

The shaken wall, read as a source

The wall that shakes solved Stokes’s oscillating wall as a problem of velocity, and found that the shear at the wall leads the wall’s own velocity by an eighth of a cycle. The source law reads the same flow as a budget, and adds a second phase to it.

A wall moving at U0cosωtU_0\cos\omega t holds, at every instant, a net vorticity of U0cosωtU_0\cos\omega t above it: the budget closes on the speed here as everywhere. The rate at which vorticity is entering is the acceleration, U0ωsinωt-U_0\omega\sin\omega t, which leads the velocity by a quarter of a cycle. And the vorticity sitting at the surface — which is the shear, and which is what the wall feels — leads by an eighth, half-way between the two, because it is the part of the budget that has entered most recently and has not yet diffused away.

So the three phases are one statement. The source runs a quarter of a cycle ahead because it is a rate; the net runs with the velocity because it is a total; and the surface value runs between them because it is a total weighted towards the recent past, with a memory whose kernel is the diffusion equation’s own. Averaged over a cycle the net vorticity above a shaken wall is zero, and the energy it sends into the fluid is not.

A floor that moves with the stream

The source law has one practical consequence that engineers arrived at without it. A model tested for ground effect sits above a floor, and a stationary floor under a moving stream grows a boundary layer that a real road or runway does not have: the air there is at rest relative to the ground, and the ground is at rest.

The fix is a belt running under the model at the stream’s speed. Read as a source, what the belt does is exact rather than approximate. Where the floor moves at the free-stream speed and the pressure along it is uniform, neither term in σ=dU/dt+(1/ρ)p/x\sigma = dU/dt + (1/\rho)\,\partial p/\partial x is non-zero — the belt is not accelerating, and there is no gradient — so the floor makes no vorticity at all. What remains is made where the model’s own pressure field reaches the floor, which is the ground effect the test exists to measure, and the belt is the only floor that makes that and nothing else.

A stationary floor under the same stream is not accelerating either. It makes its vorticity at the leading edge of the floor, where the stream first meets a surface at a different speed — a sheet put in impulsively, as a started wall puts in its speed — and then spreads it downstream as a layer. The belt removes the difference in speed, and with it the sheet.

A cylinder spun up

The flat wall has a curved relative in which the budget has a visible consequence for lift.

A spun cylinder carries its whole circulation at once, and hides it until the vorticity has left. The circulation round circles of radius r about a cylinder of radius a started spinning at once, as a share of the circulation of its own surface, 2πa²Ω, against r/a on a logarithmic axis, at νt/a² = 0.01, 0.1, 1, 10 and 100. At the surface it is the whole of it from the first instant, because no slip makes the fluid there turn with the cylinder. Just outside, the spin-up has laid down an equal and opposite ring of vorticity, so the circulation round a larger circle is only what has diffused past it: at two radii 0.000, 0.035, 0.611, 0.936 and 0.993 of the surface's at the same five times. The circulation a Magnus rotor needs is in the fluid the moment it spins; the far field learns of it only as fast as the counter-vorticity moves out.
Fig. 6 The circulation round circles of radius r about a cylinder started spinning at once, as a share of 2πa²Ω, against r/a, at νt/a² = 0.01, 0.1, 1, 10 and 100. At the surface it is the whole of it from the first instant. Just outside, an equal and opposite ring of vorticity has been laid down, so the circulation round a larger circle is only what has diffused past it: at two radii 0.000, 0.035, 0.611, 0.936 and 0.993 at the same five times.

A cylinder of radius aa starts spinning at Ω\Omega. No slip makes the fluid touching it turn with it at once, so the circulation round a circle drawn just on its surface is 2πaΩa=2πa2Ω2\pi a \cdot \Omega a = 2\pi a^2\Omega from the first instant, in any fluid.

The fluid a little further out has not moved. So the circulation round a slightly larger circle is still zero, and the difference between the two circles is the vorticity between them: the spin-up has put a thin ring of vorticity, of total strength exactly 2πa2Ω-2\pi a^2\Omega, into the fluid next to the surface. The cylinder’s own rotation and that ring add to nothing, and from far away there is no circulation at all.

Then the ring diffuses outwards. Every circle it crosses stops enclosing it, and the circulation round that circle rises towards the surface’s value. Lift with no wing at all is the Magnus effect computed from exactly that circulation — so the figure answers a question the ideal-flow calculation cannot ask, which is where a spinning cylinder’s circulation comes from. It is not built up by viscosity. It is present at the surface at once, and viscosity carries away the counter-vorticity that hides it.

The circulation arrives at each radius on the diffusion clock, and slowly after that. The circulation round a circle of radius r about a cylinder spun up at once, as a share of the circulation of its surface, against νt/a² on a logarithmic axis, at 2 radii, 5 radii and 20 radii. Half of it has arrived at 2 radii by νt/a² = 0.665, 5 radii by νt/a² = 7.75 and 20 radii by νt/a² = 143. Divided by the square of the radius those times are 0.166, 0.310 and 0.356, tending to a constant as the radius grows large against the cylinder: the square law a diffusing quantity obeys, reached once the cylinder's own size stops mattering. By νt/a² = 1000 the circulation at 2 radii is 0.999 of the wall's. Viscosity sets the clock and nothing else: the value the circulation is arriving at is the wall's, 2πa²Ω, whatever the fluid.
Fig. 7 The circulation round circles at two, five and twenty radii against νt/a² on a logarithmic axis. Half of it has arrived at two radii by νt/a² = 0.665, at five by 7.75 and at twenty by 143; divided by the square of the radius those times are 0.166, 0.310 and 0.356, tending to a constant once the radius is large against the cylinder.

The arrival is a diffusion clock. Half the circulation reaches two radii in a time of 0.665a2/ν0.665\,a^2/\nu and twenty radii in 143a2/ν143\,a^2/\nu, and the ratio of the time to the square of the radius settles towards a constant as the cylinder’s own size stops mattering. For a cylinder of ten centimetres’ radius in water that is nearly two hours to reach two radii; in a stream the counter-vorticity is carried downstream far faster than it diffuses, which is why a real rotor’s lift arrives on the flow’s time scale and not on this one. The amount it arrives at is the same either way.

What the circulation costs

Circulation is not energy, and the figure that shows the difference is the torque.

The torque settles on the steady vortex's 4πμΩa², and the fluid's angular momentum grows without end. The torque per unit length needed to keep a cylinder spinning after it is started at once, over μΩa², against νt/a², on logarithmic axes. It falls as the layer thickens and then settles: 3.59 × 4π at νt/a² = 0.01, 1.15 × 4π at νt/a² = 1 and 1.00 × 4π at νt/a² = 100. The value it settles on, 4πμΩa², is the torque of the steady flow round a spinning cylinder — a potential vortex, irrotational everywhere and still shearing, so still dissipating. Integrated over the run, the torque's impulse is 12590.571 and the angular momentum of the fluid at the end is 12590.714, in units of ρΩa⁴: the two agree to 1.1×10⁻⁵. The circulation arrives for nothing; the angular momentum does not: with the torque settled at a constant, the fluid's angular momentum grows in proportion to time for as long as fluid further out is still being set turning, and in an unbounded fluid that is for ever.
Fig. 8 The torque needed to keep the cylinder spinning, over μΩa², against νt/a². It falls as the layer thickens and then settles on 4πμΩa², the torque of the steady potential vortex. Integrated over the run, the torque’s impulse equals the angular momentum given to the fluid to a hundred-thousandth.

The torque is large while the layer is thin and falls as it thickens, as a started wall’s drag does. It does not fall to zero. It settles at 4πμΩa24\pi\mu\Omega a^2, the torque of the flow a spinning cylinder ends with — a potential vortex, whose speed falls as one over the radius, which has no vorticity anywhere and is still shearing everywhere, and so still dissipates. That is the same fact that gives a clean bubble its drag from an irrotational flow: vorticity and dissipation are not the same thing, and a flow can carry either without the other.

The calculation balances its own books. The time integral of the torque the cylinder exerts equals the angular momentum of the fluid at the end, to a hundred-thousandth, and with the torque settled at a constant the angular momentum grows in proportion to time. The circulation arrives for nothing; the angular momentum does not, and a spinning cylinder in an unbounded fluid goes on setting more distant fluid turning, and paying for it, for ever.

What the moving-wall model leaves out

Pressure gradients. Every wall here moves through fluid at rest with no pressure gradient, so the only source is the acceleration. A body moving through a fluid has both, and the two terms add; the pressure term is the one that decides separation, and the acceleration term is the one that decides what an unsteady body puts in on top of it.

Curvature and three dimensions. A flat wall and a circular cylinder keep the source a scalar. On a curved surface in three dimensions it is a vector, the surface’s own curvature adds terms, and a surface can shed vorticity pointing in directions the flat argument cannot produce.

A stream. The cylinder spins in still fluid, so its counter-vorticity can leave only by diffusion. In a stream it is convected away, and the lift a started wing takes time to reach is set by how far downstream its shed vorticity has travelled, not by how far it has diffused.

Stability. Every flow here is laminar and stays so. A started wall’s layer is stable for a long time; a cylinder spinning fast enough inside an outer boundary is not, and breaks into Taylor’s cells.

A budget with a long history

Rayleigh solved the impulsively started plate in 1911, and Stokes the oscillating one sixty years earlier, both as problems of velocity. Reading the wall as a source of vorticity, with a strength fixed by the momentum equation evaluated on the surface, is Lighthill’s framing of 1963, and the moving-wall term in it was set out explicitly by Morton in the 1980s in an account of how vorticity is generated and destroyed. The framing adds nothing to the velocity solutions. What it adds is a budget that holds for every wall motion at once, and a way of saying where a body’s circulation came from that ideal flow, which has no source at all, cannot.

Still open: the source as a vector

The flat wall and the cylinder make vorticity pointing one way only, parallel to the surface and across the flow. A surface curved in two directions — a swept wing, the hull of a ship, a bubble — makes vorticity whose direction depends on the surface’s curvature as well as on the pressure gradient and the acceleration, and part of it points along the flow. That is where the spanwise vorticity of a swept wing’s boundary layer comes from, and it is the version of this budget that three dimensions require.

Beside it is what the vorticity does once it has left the wall. Two sheets of it, or two rings, or a ring and its image in a surface, move one another at speeds fixed by their circulation alone — vortices move each other — and a shear-free surface, which cannot hold a stress, turns out to make vorticity too: a clean surface cannot refuse it wherever it is curved.

What links here

Computed from the collection rather than written here: the essays that point at this one.

Shares its objects with

Essays naming at least two of the same things, that neither author linked.

Named objects

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Angular momentumBoundary conditionCirculationImpulseKelvin's circulation theoremMagnus effectThe no-slip conditionThe Stokes layerVorticityVorticity diffusion