Viscosity

A force without the flow that makes it

A sphere carried along by a flow does not travel at the speed of the fluid at its centre. It travels at the average of the flow over its own surface — and getting that result needs no solution of the flow around the sphere at all, only the answer to a completely different problem that everybody already knows.

Worth reading first: The world with no inertia · How many things a flow must be told.

Here is a question that sounds as though it needs a calculation. A sphere is released, free of any force, in a flow that is not uniform — a pipe flow, say, where the velocity varies across the section. How fast does it go?

The answer that everybody gives, and that is wrong, is: at the speed of the fluid where the sphere is. The answer that is right requires no solution of the flow around the sphere, no boundary condition applied on its surface, and no equation solved that has not already been solved in every introductory course.

It goes at the average of the undisturbed flow over the sphere’s own surface.

What the sphere actually feels. A parabolic tube profile with a sphere sitting on the axis, drawn to scale. The sphere does not sample the velocity at its centre; it samples the whole of its own surface, and every point of that surface is off the axis, where the flow is slower. The surface average is what Faxén's law says it travels at, and for a quadratic profile the law is exact rather than approximate — the higher terms in the expansion are identically zero.
Fig. 1 Why. The sphere does not sample the velocity at a point; it presents a surface, and every part of that surface is somewhere the flow is different. In a tube every point of it is off the axis, where the fluid is slower — so the sphere is slower too, and it is slower by an amount that has nothing to do with its density and everything to do with its size.

The identity that gets it

The tool is the Lorentz reciprocal theorem, and it is the second thing linearity buys after uniqueness. For any two Stokes flows in the same region of fluid,

Su(σ^n)dS  =  Su^(σn)dS.\oint_S \mathbf{u}\cdot(\hat{\boldsymbol\sigma}\cdot\mathbf{n})\,dS \;=\; \oint_S \hat{\mathbf{u}}\cdot(\boldsymbol\sigma\cdot\mathbf{n})\,dS.

Both integrals are over the same closed surface, and in neither of them does a field appear with its own stress. The content is that the work the second flow’s stresses would do on the first flow’s velocities equals the work the first flow’s stresses would do on the second’s.

It follows in three lines from two facts and nothing else: the Stokes equations are linear, and the viscous stress tensor is symmetric. Take the divergence of uσ^\mathbf{u}\cdot\hat{\boldsymbol\sigma} and it comes out as 2μe:e^2\mu\,\mathbf{e}:\hat{\mathbf{e}}, which is symmetric in the two flows. So the difference of the two products is divergence-free, and its integral over any closed surface enclosing no singularity vanishes.

Two integrals that must agree, and do. The Lorentz reciprocal theorem tested on two point forces at different places pointing in different directions. The left column is the work the second flow's stresses would do on the first flow's velocities, integrated over a sphere containing both singularities; the right column is the same integral with the two flows exchanged. The magnitudes are printed because the test is worthless without them — a pair of flows that cannot do work on one another makes both sides zero and any relative tolerance passes.
Fig. 2 The theorem given something it could fail. Two point forces at different places pointing in different directions, the two integrals evaluated over spheres of four radii. The magnitudes are printed beside the residual for a reason set out below — a test on which both sides are zero is not a test.

The mistake that makes it look broken

The first pair chosen for that check was a translating sphere and a sphere held in a straining flow. Both are Stokes flows, both are exactly known, and both sides of the identity came out at about 10810^{-8} — differing from each other by sixty per cent.

Sixty per cent is a large number and it looks like a broken theorem. It was a degenerate pair. A translating sphere’s disturbance is a vector harmonic of degree one; a stresslet’s is of degree two; their contraction integrates to exactly zero over any sphere centred on both, by orthogonality. Both sides of the identity were zero, both were being computed as quadrature noise, and the ratio of two noises is meaningless.

The symptom is worth recognising because it looks exactly like a failure: a relative residual that is enormous and an absolute value that is tiny. The fix is to test on a pair that can do work on one another, and the magnitudes are now printed alongside so that the reader can see the test was not vacuous.

The version with no integral in it

Before using the theorem, it is worth seeing what it says in the simplest case, because that version is intuitive and the general one is not.

Apply a force at one point in a viscous fluid and measure the velocity it produces at another. Then apply the second force at the second point and measure the velocity at the first. The theorem says those two are related by

F1u2(x1)=F2u1(x2).\mathbf{F}_1\cdot\mathbf{u}_2(\mathbf{x}_1) = \mathbf{F}_2\cdot\mathbf{u}_1(\mathbf{x}_2).

Push here and measure there, and the answer is the one that pushing there and measuring here would have given. It holds for any pair of points, any pair of directions, and any bodies in between.

Push here, measure there. The reciprocal theorem's most useful consequence, with no integral in it. Apply a force at one point in a viscous fluid and measure the velocity it produces at another; then apply the second force at the second point and measure the velocity at the first. The two forces do exactly the same work on each other's velocities. It holds for any pair of points, any pair of directions, and any body in between.
Fig. 3 The mobility of a viscous fluid is symmetric, and the two numbers agree to every digit a double carries. This is the same statement as the reciprocity of an electrical network, of an elastic structure, and of an acoustic source and receiver — all of them consequences of a symmetric coefficient in a linear problem, and all of them discovered separately.

Faxén’s law, in one page

Now the payoff. Take the two flows to be the problem of interest and the problem already solved.

The problem of interest: a force-free sphere sitting in an ambient flow u\mathbf{u}^\infty, which satisfies the Stokes equations on its own and is whatever the pipe or the shear was doing before the sphere arrived.

The auxiliary problem: the same sphere translating at unit speed through fluid at rest, whose answer is Stokes’ 6πμa6\pi\mu a and is the first thing anybody computes.

Apply the identity on the sphere’s surface. On it, the real flow’s velocity is the sphere’s own rigid translation, and the auxiliary flow’s traction is uniform — Stokes drag is distributed uniformly over a sphere, which is the special fact that makes this work. Everything collapses, and what is left is

U=uS+F6πμa,\mathbf{U} = \langle \mathbf{u}^\infty \rangle_S + \frac{\mathbf{F}}{6\pi\mu a},

the surface average plus whatever an applied force would contribute. For a force-free particle the second term is zero and the first is the whole answer.

The surface average has a closed form for anything with a Taylor series. Expanding the ambient about the sphere’s centre, the odd moments vanish by symmetry and the second moment of a sphere is a2δij/3a^2\delta_{ij}/3, so

uS=u(0)+a262u+O(a4).\langle \mathbf{u}^\infty \rangle_S = \mathbf{u}^\infty(0) + \frac{a^2}{6}\nabla^2\mathbf{u}^\infty + O(a^4).

For an ambient flow that is quadratic — Poiseuille is — the remainder is identically zero, and the law is exact rather than asymptotic.

The number, in a tube

In a round tube the ambient is u=umax(1r2/R2)u = u_{\max}(1 - r^2/R^2) and its Laplacian is 4umax/R2-4u_{\max}/R^2, everywhere, with no dependence on position. So the correction does not depend on where in the tube the particle is. Only on how big it is.

U=u(rc)23a2R2umax.U = u(r_c) - \frac{2}{3}\,\frac{a^2}{R^2}\,u_{\max}.

A sphere does not go at the speed of the flow it is in. How far a force-free sphere on the axis of a round tube lags the fluid at its own centre, against its size. The lag is two-thirds of the square of the size ratio and comes from the reciprocal theorem in one line: the sphere moves at the average of the ambient flow over its own surface, and a parabolic profile is slower everywhere on that surface than at the middle. At a fifth of the tube's radius the lag is 2.7 per cent, which is the difference between a tracer and a thing being measured.
Fig. 4 How far a sphere on the axis lags the fluid at its own centre, against its size. Two-thirds of the square of the ratio: 0.7 per cent for a particle a tenth of the radius, 2.7 per cent at a fifth, six per cent at three-tenths. Small, and always of one sign — it does not average away over a population.

That number is the difference between a tracer and a thing being measured, and it is a systematic error rather than a scatter. A velocimetry technique that seeds a pipe with particles of a known size can correct for it exactly; one that seeds with a distribution of sizes cannot, because the correction goes as the square of the radius and the mean of a square is not the square of the mean.

What it costs to be wrong about this

The lag is a fraction of a per cent for the particles velocimetry actually uses, and it would be fair to ask why it is worth a page. Three reasons, and the third is the one that decides it.

It is systematic. Random error in a velocity measurement falls as the square root of the number of particles. This does not fall at all: every particle in the field is slow, all of them by the same fraction of their local velocity, and averaging a million of them gives the same wrong answer with a smaller error bar on it.

It is largest where the gradients are. The correction is the Laplacian of the ambient, so it vanishes in a uniform flow, vanishes in a simple shear — a shear is linear, and a linear field has no Laplacian — and is largest exactly where a measurement is most interesting, which is in a boundary layer or a shear layer. A technique validated in a free stream is validated where the effect is zero.

And it has the wrong sign for the thing it is usually used to find. Seeding a boundary layer with particles and reading their speeds gives a profile that is systematically slow near the wall, where the curvature is greatest. The wall shear stress inferred from it is therefore systematically low, and the drag it implies is low with it — an error in the conservative direction for a lift estimate and the dangerous direction for a drag one.

What the sphere actually feels. A parabolic tube profile with a sphere sitting on the axis, drawn to scale. The sphere does not sample the velocity at its centre; it samples the whole of its own surface, and every point of that surface is off the axis, where the flow is slower. The surface average is what Faxén's law says it travels at, and for a quadratic profile the law is exact rather than approximate — the higher terms in the expansion are identically zero.
Fig. 5 The same picture at a particle three-tenths of the tube’s radius. At this size the effect is six per cent, the “point” the particle is supposed to be measuring is a substantial fraction of the apparatus, and the wall correction the law does not include has become comparable with the term it does.

What else falls out of the same identity

Faxén’s is the tidy application; the theorem’s real value is how many other things it does without any new solve.

A drag from a slightly different shape. Deform a sphere a little and the change in its drag can be had from the undeformed sphere’s traction integrated against the deformation, with no solution of the deformed problem at all. That is Brenner’s result and it is the standard way small departures from sphericity are priced.

A swimming speed without solving for the swimmer. A body that deforms its own surface moves at a velocity that is a surface integral of that deformation weighted by the traction of the towed problem. Taylor’s waving sheet can be got this way, and so can the general result that a time-reversible stroke goes nowhere.

And a suspension’s viscosity. The extra stress a rigid particle contributes to a sheared fluid is its stresslet, and the stresslet is what the reciprocal theorem extracts from the straining problem. Einstein’s five halves is one of these integrals.

The two problems the theorem puts together. On the left, a sphere towed through fluid at rest — the problem every fluids course solves first, and the one whose answer is 6πμaU. On the right, a rigid sphere held still in a pure straining flow, which is the problem Einstein's viscosity is made of. The reciprocal theorem relates the two without either being solved again, and it is the first of them that supplies the answer to the second.
Fig. 6 The two auxiliary problems this collection now leans on. The left-hand one — a sphere towed through still fluid — supplies the answer to Faxén’s question. The right-hand one supplies the answer to the suspension question. Neither is a hard calculation, and between them they price a great deal that looks as though it needs a new solve.

Symmetry of the resistance matrix, and why a bacterium can swim

The mobility statement above — push here, measure there — has a compact form for a whole body, and the compact form contains a result worth more than the identity that produced it.

A rigid body in Stokes flow relates the force and torque on it to its translation and rotation through a single matrix,

(FT)=μ(ACTCB)(UΩ),\begin{pmatrix}\mathbf{F}\\ \mathbf{T}\end{pmatrix} = -\mu \begin{pmatrix} \mathsf{A} & \mathsf{C}^{\mathsf{T}} \\ \mathsf{C} & \mathsf{B}\end{pmatrix} \begin{pmatrix}\mathbf{U}\\ \boldsymbol{\Omega}\end{pmatrix},

and the reciprocal theorem is exactly the statement that this matrix is symmetric. Six by six, twenty-one independent entries rather than thirty-six, and the symmetry is not an approximation.

The diagonal blocks are familiar: A\mathsf{A} is the drag, 6πa6\pi a for a sphere, and B\mathsf{B} is the rotational drag, 8πa38\pi a^3. It is the off-diagonal block that carries the interesting content. C\mathsf{C} couples torque to translation and, by the symmetry, couples force to rotation with the same coefficient. Spin the body and it moves; push it and it spins; and the two effects have one number between them rather than two.

A body with any mirror symmetry has C=0\mathsf{C} = 0 identically. A sphere, an ellipsoid, a disc, a rod: spin any of them about any axis and they stay where they are, however fast and however long. The coupling is non-zero only for a body that is chiral — a helix, a corkscrew, a body with a handed twist and no plane of reflection.

Which is the whole of how a bacterium swims. A flagellum is a rigid helix turned by a rotary motor in the cell wall, at a hundred revolutions a second or so, and the helix’s coupling coefficient converts that rotation into a thrust. Nothing about the motion is reciprocal in time, because rotation is not a reciprocal stroke: reverse it and the organism goes backwards, which is exactly what a stroke that undoes itself cannot do. The cell body counter-rotates to balance the torque, and the swimming speed follows from the two resistance matrices solved together, at a few tens of microns a second for the numbers a bacterium has.

The symmetry then makes a prediction that is easy to test and slightly startling. Because C\mathsf{C} is shared, towing the same helix through the fluid must make it rotate, at a rate fixed by the same coefficient that governs its propulsion. A corkscrew dragged through syrup turns itself, and how fast it turns per unit towing speed equals how fast it advances per unit imposed spin. Two experiments, one number, and the equality is a theorem rather than a coincidence.

And the handedness matters exactly as it should. A left-handed helix rotated the same way as a right-handed one swims in the opposite direction, because C\mathsf{C} changes sign under reflection — which is why artificial magnetic microswimmers are manufactured with a specified handedness, and why their direction is reversed by reversing the field’s rotation rather than by anything about the fluid. Propulsion at zero Reynolds number is a property of a body’s chirality, and the reason one number describes both of its faces is the symmetry this essay’s identity establishes.

Two spheres, and why suspensions are hard

There is one more thing the theorem gives cheaply and it is the reason a suspension of particles is not a simple problem.

Two spheres settling side by side in a viscous fluid fall faster than either would alone, because each one is falling through the downwash of the other. The reciprocal theorem, applied to the pair, gives the leading interaction without solving the two-sphere problem: it is the Stokeslet of one evaluated at the other, and it decays as 1/r1/r — the slowest decay of any interaction in physics that is not electrostatic.

That slowness is the whole difficulty. A pair correction that fell as 1/r31/r^3 would be a neighbour effect and a suspension would be a gas of independent particles with a small correction. A correction that falls as 1/r1/r is not a neighbour effect at all: summing it over a uniform distribution of particles gives an integral that diverges, and making it converge takes an argument about the suspension as a whole rather than about pairs.

So the dilute limit of a suspension is not the limit of few neighbours; it is the limit of few particles per volume, however far apart they are. That is why Einstein’s coefficient stops being the measurement at a few per cent by volume rather than at a few tens, and why the second term in the expansion took another sixty years to compute.

Why it stops the moment there is inertia

Every step of the proof used the linearity of the Stokes equations, and the nonlinear term destroys all of it. There is no reciprocal theorem for the Navier–Stokes equations, and the reason is easy to state: reciprocity is a symmetry, and the convective term breaks it by picking a direction — the direction the fluid is going.

The practical boundary is the same one creeping flow itself sits inside, which is a good deal lower than a Reynolds number of one. A particle in a tube at Re = 0.1 is well inside it; the same particle at Re = 10 is not, and its lag is then a different and much harder problem with a lift force in it as well.

Particles at St = 0.3, against the flow that carries themParticle paths and the streamlines they were released on, in this site's exact cylinder solution. At small Stokes number the two are indistinguishable and the body catches nothing; as the particles get heavier their paths straighten, cross the streamlines, and begin to strike. The paths are integrated with Stokes drag and nothing else — no gravity, no lift, no effect of the particles on the flow.St = 0.31 of 11 released paths strike the bodycollection efficiency 7.1%Stokes drag on a particle, integrated through the exact ideal cylinder solutionSt = 0.3 · any Reynolds number for the flow; the particle drag is Stokesian
Fig. 7 And the other reason a particle does not follow a flow: inertia of its own. A particle whose density differs from the fluid’s has a relaxation time and lags a changing flow for a completely separate reason, which this collection prices in the essay on tracers. Faxén’s lag is present even for a particle of exactly the fluid’s density in a perfectly steady flow, and the two add.

What the picture cannot show

The tube wall is outside the theorem. Faxén’s law is derived for a sphere in an unbounded fluid, and the ambient it uses is whatever the flow was doing before the sphere arrived. Putting a wall a few radii away adds a correction of the opposite sign and of order (a/R)3(a/R)^3 on the axis — separable from the (a/R)2(a/R)^2 term over the range drawn here, and not separable beyond about a third.

The particle is rigid and spherical. A deformable drop obeys a different law with its viscosity ratio in it, and a non-spherical particle rotates as well as translating, which brings in a second Faxén law for the angular velocity that is not drawn here.

And nothing here is Brownian. A particle small enough for the surface-average correction to be negligible is usually small enough for thermal motion to dominate its trajectory entirely, which is a different subject with a different mathematics.

How much of the fore-and-aft symmetry survives. A measure of how different the flow in front of a cylinder is from the flow behind it, against Reynolds number. Creeping flow is exactly symmetric because it is reversible; the grid solve is nearly so at Reynolds number 1 and not at all by 100, and the difference is the wake.
Fig. 8 The property of Stokes flow that everything in this essay depends on, drawn directly: the fore-and-aft symmetry that linearity forces. A creeping flow reversed is the same flow reversed, exactly, and the reciprocal theorem is that statement made about a pair of flows instead of about one.

Who found it, and when

Lorentz gave the theorem in 1896, in a paper largely about something else, and it sat almost unused for fifty years. Faxén derived his laws in 1922 by a direct expansion rather than by reciprocity — the reciprocal derivation, which is the one above and is a page rather than a chapter, came later. The modern use of the theorem as a general-purpose tool for getting forces without flows dates from the 1960s and is largely Brenner’s.

The surprising connection is with a piece of applied mathematics that is not fluid mechanics at all. The result that a sphere samples the average of a field over its surface rather than the field at its centre, with the correction being the Laplacian times a2/6a^2/6, is the same statement as the mean value property of harmonic functions and its failure for functions that are not harmonic. A sphere in a viscous fluid is, to that order, an instrument that measures the spherical mean — and the correction it makes is exactly the amount by which the ambient fails to be harmonic.

Where the ladder goes next

Beside this rung is the minimum-dissipation theorem, which is the other thing linearity buys, and which fails at the same place for the same reason. Above it are the two applications this collection now makes of the identity: what a suspension does to a viscosity and a swimmer that cannot go backwards.

Below it is the world with no inertia, which is the regime all of this holds in and only in, and how many things a flow must be told, which is where the boundary conditions the theorem contracts against come from.

What links here

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

Reads more easily once this is understood

Essays that name this one as worth reading first.

Shares its objects with

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

Named objects

A dashed tag is an object no other essay names yet.

Boundary conditionCreeping flowDragLinearityMeasurementParticleReciprocityStokes flowStressletTracer