Rayleigh Acoustic Streaming Above a Vibrating Surface

Contents
  1. What is quoted here
  2. Why the effect cannot appear before second order
  3. The first-order Stokes layer
  4. The second-order mean flow and the slip velocity
  5. The direction of the circulation over a plate
  6. The same mechanism in Kundt's tube
  7. What is not derived here

This appendix supplies the derivation owed at Phenomenon 39.8 of Experiment: Waves and Acoustics: the steady second-order flow that an oscillating boundary drives in the fluid above it, and the direction of its outer branch, which is what carries a light powder to the antinodes of a sounding plate where sand collects at the nodes [Faraday:1831] [Chladni:1787].

The scope is fixed in advance by Remark 39.9 of the chapter and is not widened here. What is derived is the streaming velocity, its coefficient, and the sense of the circulation. What is not derived is a threshold grain radius separating sand from lycopodium: that comparison turns on the grain's adhesion to the plate, which this treatise does not model. The reader should hold the chapter's bound in view throughout, because the calculation below is exact enough to invite being pushed further than it can go.

What is quoted here

No theorem. The whole argument is an expansion of the incompressible Navier–Stokes equations Equation (35.32) of Fluid Dynamics in the amplitude of the motion, and every step — the linear boundary-layer solution, the time averages, and five elementary integrals — is carried out here.

Three things are assumed rather than proved, and all three are statements about the physical regime rather than about mathematics. The fluid is treated as incompressible within a plate wavelength, which requires the acoustic wavelength in air to be much the longer of the two (Lemma A66.5 states the condition and Example A66.7 checks it). The motion is assumed to have settled into a state that is steady in the mean, so that \(\avg{\pp_{t}\vect{v}_{2}}=0\). And the expansion is assumed to be asymptotic in the amplitude, which is the usual and unproved status of such expansions in fluid mechanics.

The result derived below is Rayleigh's, published in 1884 in the Philosophical Transactions under the title “On the circulation of air observed in Kundt's tubes, and on some allied acoustical problems”. That paper has no key in references.bibRayleigh:1883 there is the paper on the equilibrium of a heavy fluid of variable density, a different work, and citing it here would be exactly the misattribution the editorial rules warn against — so the attribution is made in words, on the footing of Darboux's memoir in Remark A12.15. Nothing below rests on it.

Why the effect cannot appear before second order

Write \(\avg{\cdot}\) for the average over one period \(2\pi/\omega\) of the driving, and expand every field in the dimensionless amplitude \(\epsilon\) of the boundary motion:

\begin{equation}\tag{A66.1} \vect{v}=\epsilon\,\vect{v}_{1}+\epsilon^{2}\vect{v}_{2}+\cdots\ec \qquad p=p_{0}+\epsilon\,p_{1}+\epsilon^{2}p_{2}+\cdots\ep \end{equation}

At first order the equations are linear with coefficients independent of \(t\) and the forcing is \(\propto\cos\omega t\), so every first-order field is a harmonic function of time of the same frequency and

\begin{equation}\tag{A66.2} \avg{\vect{v}_{1}}=0\ep \end{equation}

A tracer carried by the fluid therefore returns, at first order, to where it started after each period: there is no steady transport whatever. Steady transport first appears at order \(\epsilon^{2}\), and it appears there because the average of a product of two oscillating quantities of the same frequency need not vanish even though each factor averages to zero. That is the entire physical content of the phenomenon, and it is why Phenomenon 39.8 cannot be obtained from any first-order acoustic quantity, however cleverly combined.

The first-order Stokes layer

Proposition A66.1 (The oscillating boundary layer).

Let a plane wall occupy \(y=0\) with fluid in \(y>0\), and let the outer acoustic field impose, just outside the layer, the tangential velocity \(u_{\infty}=U(x)\cos\omega t\), with \(U\) varying on a length scale much greater than the layer thickness. Then the first-order velocity satisfying no slip at the wall is

\begin{equation}\tag{A66.3} u_{1}=U(x)\left[\cos\omega t -\ee^{-\eta}\cos\left(\omega t-\eta\right)\right]\ec \qquad \eta:=\frac{y}{\delta}\ec \end{equation}

with the Stokes-layer thickness

\begin{equation}\tag{A66.4} \delta:=\sqrt{\frac{2\nu}{\omega}}\ec \end{equation}

in \(\mathrm{m}\), and the wall-normal component follows from continuity as

\begin{equation}\tag{A66.5} v_{1}=-\dv{U}{x}\,\delta\, \Re\left[H(\eta)\,\ee^{\ii\omega t}\right]\ec\qquad H(\eta):=\eta-\frac{h(\eta)}{1+\ii}\ec \end{equation}

where \(h(\eta):=1-E(\eta)\) and \(E(\eta):=\ee^{-\left(1+\ii\right)\eta}\), so that \(u_{1}=U\,\Re\left[h\,\ee^{\ii\omega t}\right]\). Rests on Equations (35.32) and (A66.1).

Proof.

Derives Proposition A66.1. At first order Equation (35.32) linearizes to \(\pp_{t}u_{1}=-\rho^{-1}\pp_{x}p_{1}+\nu\,\pp_{y}^{2}u_{1}\), the convective terms being of second order and the streamwise viscous term smaller than the transverse one by the square of the ratio of the layer thickness to the scale of \(U\). The outer field carries no shear, so it satisfies \(\pp_{t}u_{\infty}=-\rho^{-1}\pp_{x}p_{1}\); and by Equation (A66.1) applied to the pressure together with the thinness of the layer, \(p_{1}\) has the same value inside the layer as just outside it. Subtracting,

\begin{equation}\tag{A66.6} \pp_{t}\left(u_{1}-u_{\infty}\right) =\nu\,\pp_{y}^{2}\left(u_{1}-u_{\infty}\right)\ec \end{equation}

since \(\pp_{y}^{2}u_{\infty}=0\). Seek \(u_{1}-u_{\infty} =\Re\left[A(x)\,\ee^{\ii\omega t}\ee^{-\gamma y}\right]\): then \(\ii\omega=\nu\gamma^{2}\), so \(\gamma=\sqrt{\ii\omega/\nu}=\left(1+\ii\right)/\delta\) with \(\delta\) as in Equation (A66.4), the root with positive real part being the one that decays. No slip at \(y=0\) requires \(u_{1}=0\) there, so \(A=-U(x)\) and

\begin{equation}\tag{A66.7} u_{1}=U\,\Re\left[\left(1-\ee^{-\left(1+\ii\right)\eta}\right) \ee^{\ii\omega t}\right] =U\,\Re\left[h\,\ee^{\ii\omega t}\right]\ec \end{equation}

and expanding the real part with \(\ee^{-\left(1+\ii\right)\eta}\ee^{\ii\omega t} =\ee^{-\eta}\ee^{\ii\left(\omega t-\eta\right)}\) gives Equation (A66.3).

For \(v_{1}\), integrate continuity \(\pp_{x}u_{1}+\pp_{y}v_{1}=0\) upward from the wall, where \(v_{1}=0\):

\begin{equation}\tag{A66.8} v_{1}=-\int_{0}^{y}\pp_{x}u_{1}\,\dd y' =-\dv{U}{x}\,\delta\, \Re\left[\ee^{\ii\omega t}\int_{0}^{\eta}h\,\dd\eta'\right]\ec \end{equation}

and

\begin{equation}\tag{A66.9} \int_{0}^{\eta}h\,\dd\eta' =\int_{0}^{\eta}\left(1-\ee^{-\left(1+\ii\right)\eta'}\right) \dd\eta' =\eta-\frac{1-E}{1+\ii} =\eta-\frac{h}{1+\ii}=H\ec \end{equation}

which is Equation (A66.5). Note that \(v_{1}\) carries the factor \(\dd U/\dd x\): a spatially uniform oscillation drives no normal motion, and it will drive no streaming either.

The second-order mean flow and the slip velocity

Lemma A66.2 (The layer is driven by the excess Reynolds stress).

Let \(\avg{u_{2}}\) be the time-averaged second-order streamwise velocity. Then, to leading order in the thinness of the layer,

\begin{equation}\tag{A66.10} \mu\,\pp_{y}^{2}\avg{u_{2}}=F(y)\ec\qquad F:=\rho\left[ \avg{u_{1}\pp_{x}u_{1}+v_{1}\pp_{y}u_{1}} -\avg{u_{\infty}\pp_{x}u_{\infty}}\right]\ec \end{equation}

with \(\avg{u_{2}}=0\) at \(y=0\) and \(\pp_{y}\avg{u_{2}}\to0\) as \(\eta\to\infty\). Consequently

\begin{equation}\tag{A66.11} u_{s}:=\lim_{\eta\to\infty}\avg{u_{2}} =-\frac{1}{\mu}\int_{0}^{\infty}y\,F(y)\,\dd y\ep \end{equation}

Rests on Proposition A66.1, Equation (35.32) and Equation (A66.2).

Proof.

Derives Lemma A66.2. Take the streamwise component of Equation (35.32) at order \(\epsilon^{2}\) and average over a period. The unsteady term averages to zero in a state steady in the mean; the convective terms contribute \(\avg{u_{1}\pp_{x}u_{1}+v_{1}\pp_{y}u_{1}}\), since the second-order velocity's own convection is of fourth order; and of the viscous term only \(\nu\,\pp_{y}^{2}\avg{u_{2}}\) survives, by the same comparison of transverse with streamwise gradients used in Proposition A66.1. Hence

\begin{equation}\tag{A66.12} \mu\,\pp_{y}^{2}\avg{u_{2}} =\rho\avg{u_{1}\pp_{x}u_{1}+v_{1}\pp_{y}u_{1}} +\pp_{x}\avg{p_{2}}\ep \end{equation}

Now evaluate the same equation just outside the layer, where the field is the irrotational \(u_{\infty}\) and there is no mean shear. There

\begin{equation}\tag{A66.13} 0=\rho\avg{u_{\infty}\pp_{x}u_{\infty}}+\pp_{x}\avg{p_{2}}\ec \end{equation}

that is, the Reynolds stress of an irrotational oscillation is balanced entirely by the second-order mean pressure and drives nothing. The layer is thin, so \(\avg{p_{2}}\) is the same function of \(x\) inside it as immediately outside; subtracting Equation (A66.13) from Equation (A66.12) eliminates the pressure and leaves Equation (A66.10). By construction \(F\to0\) as \(\eta\to\infty\), and exponentially, since \(u_{1}\to u_{\infty}\) exponentially.

For the boundary conditions: no slip holds at every order, so \(\avg{u_{2}}(0)=0\); and the mean shear at the outer edge of the layer belongs to the outer streaming, which varies on the acoustic length scale rather than on \(\delta\) and is therefore negligible here. Then integrating Equation (A66.10) downward from infinity, \(\mu\,\pp_{y}\avg{u_{2}}(y)=-\int_{y}^{\infty}F\,\dd y'\), and integrating that upward from the wall,

\begin{equation}\tag{A66.14} \mu\,u_{s} =-\int_{0}^{\infty}\!\!\int_{y}^{\infty}F(y')\,\dd y'\,\dd y =-\int_{0}^{\infty}F(y')\int_{0}^{y'}\dd y\,\dd y' =-\int_{0}^{\infty}y'F(y')\,\dd y'\ec \end{equation}

the exchange of the order of integration being legitimate because \(F\) decays exponentially. That is Equation (A66.11).

Theorem A66.3 (Rayleigh's limiting velocity).

With \(U\) and \(\delta\) as above,

\begin{equation}\tag{A66.15} u_{s}=-\frac{3}{4\omega}\,U\dv{U}{x} =-\frac{3}{4\omega}\dv{\avg{u_{\infty}^{2}}}{x}\ec \end{equation}

in \(\mathrm{m}/\mathrm{s}\). The viscosity has cancelled: \(u_{s}\) does not contain \(\nu\), and the thickness \(\delta\) of the layer that produced it does not appear. Rests on Lemma A66.2, Equation (A66.3) and Equation (A66.5).

Proof.

Derives Theorem A66.3. Write \(g(\eta,t):=\Re\left[h\,\ee^{\ii\omega t}\right]\) and \(G(\eta,t):=\Re\left[H\,\ee^{\ii\omega t}\right]\), so that by Proposition A66.1

\begin{equation}\tag{A66.16} u_{1}=Ug\ec\qquad \pp_{x}u_{1}=U'g\ec\qquad \pp_{y}u_{1}=\frac{U}{\delta}\pp_{\eta}g\ec\qquad v_{1}=-U'\delta\,G\ec \end{equation}

with \(U'=\dd U/\dd x\). The two Reynolds-stress terms are therefore

\begin{equation}\tag{A66.17} \avg{u_{1}\pp_{x}u_{1}}=UU'\avg{g^{2}}\ec\qquad \avg{v_{1}\pp_{y}u_{1}}=-UU'\avg{G\,\pp_{\eta}g}\ec \end{equation}

the factor \(\delta\) cancelling between \(v_{1}\) and \(\pp_{y}u_{1}\) — which is already the reason the answer will not contain the layer thickness. Since \(\avg{u_{\infty}\pp_{x}u_{\infty}}=UU'\avg{\cos^{2}\omega t} =\tfrac{1}{2}UU'\),

\begin{equation}\tag{A66.18} F=\rho\,UU'\,\Psi(\eta)\ec\qquad \Psi:=\avg{g^{2}}-\avg{G\,\pp_{\eta}g}-\tfrac{1}{2}\ep \end{equation}

Evaluating \(\Psi\). For two quantities written as \(\Re\left[A\ee^{\ii\omega t}\right]\) and \(\Re\left[B\ee^{\ii\omega t}\right]\) the period average of the product is \(\tfrac{1}{2}\Re\left[A\bar{B}\right]\). With \(\pp_{\eta}g=\Re\left[h'\ee^{\ii\omega t}\right]\) and \(h'=\left(1+\ii\right)E\),

\begin{equation}\tag{A66.19} 2\Psi=\abs{h}^{2}-1-\Re\left[H\overline{h'}\right]\ep \end{equation}

Now \(h=1-E\) with \(E=\ee^{-\eta}\ee^{-\ii\eta}\), so

\begin{equation}\tag{A66.20} \abs{h}^{2}-1=-2\Re E+\abs{E}^{2} =-2\ee^{-\eta}\cos\eta+\ee^{-2\eta}\ec \end{equation}

and, using \(\overline{h'}=\left(1-\ii\right)\bar{E}\) together with \(\left(1-\ii\right)/\left(1+\ii\right)=-\ii\),

\begin{equation}\tag{A66.21} H\overline{h'} =\left[\eta-\frac{1-E}{1+\ii}\right]\left(1-\ii\right)\bar{E} =\eta\left(1-\ii\right)\bar{E}+\ii\bar{E}-\ii\abs{E}^{2}\ep \end{equation}

Taking real parts with \(\bar{E}=\ee^{-\eta} \left(\cos\eta+\ii\sin\eta\right)\),

\begin{equation}\tag{A66.22} \Re\left[H\overline{h'}\right] =\eta\ee^{-\eta}\left(\cos\eta+\sin\eta\right) -\ee^{-\eta}\sin\eta\ec \end{equation}

the last term of Equation (A66.21) being purely imaginary. Assembling Equations (A66.20) and (A66.22),

\begin{equation}\tag{A66.23} 2\Psi=-2\ee^{-\eta}\cos\eta+\ee^{-2\eta} -\eta\ee^{-\eta}\left(\cos\eta+\sin\eta\right) +\ee^{-\eta}\sin\eta\ep \end{equation}

The moment. By Equations (A66.11) and (A66.18), with \(y=\delta\eta\),

\begin{equation}\tag{A66.24} u_{s}=-\frac{\rho UU'\delta^{2}}{\mu} \int_{0}^{\infty}\eta\,\Psi\,\dd\eta =-\frac{2UU'}{\omega}\int_{0}^{\infty}\eta\,\Psi\,\dd\eta\ec \end{equation}

since \(\rho\delta^{2}/\mu=\delta^{2}/\nu=2/\omega\) by Equation (A66.4). The required integrals follow from

\begin{equation}\tag{A66.25} \int_{0}^{\infty}\eta^{n}\ee^{-\eta}\ee^{\ii\eta}\,\dd\eta =\frac{n!}{\left(1-\ii\right)^{n+1}}\ec \end{equation}

with \(\left(1-\ii\right)^{2}=-2\ii\) and \(\left(1-\ii\right)^{3}=-2-2\ii\). For \(n=1\) the right-hand side is \(1/\left(-2\ii\right)=\ii/2\), so

\begin{equation}\tag{A66.26} \int_{0}^{\infty}\eta\ee^{-\eta}\cos\eta\,\dd\eta=0\ec\qquad \int_{0}^{\infty}\eta\ee^{-\eta}\sin\eta\,\dd\eta=\tfrac{1}{2}\ec \end{equation}

and for \(n=2\) it is \(2/\left(-2-2\ii\right)=-1/\left(1+\ii\right) =\left(-1+\ii\right)/2\), so

\begin{equation}\tag{A66.27} \int_{0}^{\infty}\eta^{2}\ee^{-\eta}\cos\eta\,\dd\eta =-\tfrac{1}{2}\ec\qquad \int_{0}^{\infty}\eta^{2}\ee^{-\eta}\sin\eta\,\dd\eta =\tfrac{1}{2}\ec \end{equation}

while \(\int_{0}^{\infty}\eta\,\ee^{-2\eta}\dd\eta=\tfrac{1}{4}\). Multiplying Equation (A66.23) by \(\eta\) and integrating term by term,

\begin{equation}\tag{A66.28} 2\int_{0}^{\infty}\eta\,\Psi\,\dd\eta =-2\cdot 0+\tfrac{1}{4} -\left(-\tfrac{1}{2}+\tfrac{1}{2}\right)+\tfrac{1}{2} =\tfrac{3}{4}\ec \end{equation}

so \(\int_{0}^{\infty}\eta\Psi\,\dd\eta=\tfrac{3}{8}\) and Equation (A66.24) gives \(u_{s}=-\left(2/\omega\right)\left(3/8\right)UU'\), which is the first member of Equation (A66.15). The second member follows from \(\avg{u_{\infty}^{2}}=\tfrac{1}{2}U^{2}\), whose \(x\) derivative is \(UU'\).

Proposition A66.4 (The inner counter-flow).

The mean flow at the wall itself runs the other way. Its shear there is

\begin{equation}\tag{A66.29} \left(\pp_{y}\avg{u_{2}}\right)_{y=0} =\frac{1}{2\omega\delta}\,U\dv{U}{x}\ec \end{equation}

which has the sign of \(U\,\dd U/\dd x\), opposite to that of \(u_{s}\) in Equation (A66.15). The mean profile therefore reverses once within the layer, at a height of order \(\delta\). Rests on Lemma A66.2, Equation (A66.23) and Theorem A66.3.

Proof.

Derives Proposition A66.4. From the proof of Lemma A66.2, \(\mu\left(\pp_{y}\avg{u_{2}}\right)_{y=0} =-\int_{0}^{\infty}F\,\dd y =-\rho UU'\delta\int_{0}^{\infty}\Psi\,\dd\eta\). The zeroth moments needed are \(\int_{0}^{\infty}\ee^{-\eta}\cos\eta\,\dd\eta =\int_{0}^{\infty}\ee^{-\eta}\sin\eta\,\dd\eta=\tfrac{1}{2}\), from Equation (A66.25) at \(n=0\), together with \(\int_{0}^{\infty}\ee^{-2\eta}\dd\eta=\tfrac{1}{2}\) and Equation (A66.26). Integrating Equation (A66.23),

\begin{equation}\tag{A66.30} 2\int_{0}^{\infty}\Psi\,\dd\eta =-2\cdot\tfrac{1}{2}+\tfrac{1}{2} -\left(0+\tfrac{1}{2}\right)+\tfrac{1}{2}=-\tfrac{1}{2}\ec \end{equation}

so \(\int_{0}^{\infty}\Psi\,\dd\eta=-\tfrac{1}{4}\) and \(\mu\left(\pp_{y}\avg{u_{2}}\right)_{y=0} =\tfrac{1}{4}\rho\delta UU'\). Dividing by \(\mu=\rho\nu\) and using \(\nu=\omega\delta^{2}/2\) gives Equation (A66.29). Since \(\avg{u_{2}}\) starts from zero at the wall with a shear of one sign and ends at \(u_{s}\) of the other, it changes sign once, at a height that the explicit profile places within a small multiple of \(\delta\).

The direction of the circulation over a plate

Everything so far holds for any oscillating tangential field. To reach Phenomenon 39.8 one further step is needed, and it is the step at which the answer is decided: the relation between the tangential air velocity \(U(x)\) and the plate's normal motion.

Lemma A66.5 (The tangential field above a bending plate).

Let the plate vibrate with normal velocity \(v\left(x,0,t\right)=V_{0}\sin\left(k_{p}x\right)\cos\omega t\), so that its nodal lines are at \(\sin\left(k_{p}x\right)=0\) and its antinodes midway between them. Suppose the bending wavelength is much shorter than the acoustic wavelength in the fluid, \(k_{p}\gg\omega/c\), and much longer than the Stokes layer, \(k_{p}\delta\ll1\). Then the air motion within a bending wavelength is incompressible and irrotational, with

\begin{equation}\tag{A66.31} \phi=-\frac{V_{0}}{k_{p}}\sin\left(k_{p}x\right) \ee^{-k_{p}y}\cos\omega t\ec \end{equation}

and the tangential velocity imposed on the layer is

\begin{equation}\tag{A66.32} U(x)=-V_{0}\cos\left(k_{p}x\right)\ep \end{equation}

Its magnitude is therefore greatest over the plate's nodal lines and vanishes over its antinodes. Rests on Proposition 35.28, Equation (35.25) and Equation (A66.4).

Proof.

Derives Lemma A66.5. When \(k_{p}\gg\omega/c\) the compressible wave equation for the velocity potential, \(\nabla^{2}\phi=c^{-2}\pp_{t}^{2}\phi\), reduces within a bending wavelength to Equation (35.25), because the term on the right is smaller than \(\pp_{x}^{2}\phi\) by \(\left(\omega/ck_{p}\right)^{2}\). Separating with the \(x\) dependence imposed by the plate and requiring decay as \(y\to\infty\) gives \(\phi\propto\sin\left(k_{p}x\right)\ee^{-k_{p}y}\), and \(\nabla^{2}\phi=\left(-k_{p}^{2}+k_{p}^{2}\right)\phi=0\) confirms it. Fixing the constant by \(\pp_{y}\phi=v\left(x,0,t\right)\) at \(y=0\) gives Equation (A66.31), whence

\begin{equation}\tag{A66.33} u=\pp_{x}\phi =-V_{0}\cos\left(k_{p}x\right)\ee^{-k_{p}y}\cos\omega t\ep \end{equation}

Since \(k_{p}\delta\ll1\), the exponential is indistinguishable from unity across the Stokes layer, so the field Equation (A66.33) is what Proposition A66.1 sees as \(u_{\infty}\), and Equation (A66.32) follows.

The physical reading is worth one sentence, because the result is the opposite of the naive guess. Over an antinode the plate pushes air straight up and down and the horizontal motion vanishes by symmetry; over a nodal line the plate does not move at all, but the air expelled from the antinode on one side must cross to the other, and it is there that the horizontal velocity is greatest.

Corollary A66.6 (The powder collects at the antinodes).

With Equation (A66.32), Equation (A66.15) gives

\begin{equation}\tag{A66.34} u_{s}=\frac{3V_{0}^{2}k_{p}}{8\omega} \sin\left(2k_{p}x\right)\ec \end{equation}

which is directed from each nodal line towards the antinodes on either side of it. The outer branch of the circulation therefore sweeps the fluid just above the layer from the nodes to the antinodes, rising there and returning above; a grain carried by that branch collects at the antinodes, where sand does not, which is Phenomenon 39.8. Rests on Theorem A66.3, Lemma A66.5 and Phenomenon 39.5.

Proof.

Derives Corollary A66.6. \(U^{2}=V_{0}^{2}\cos^{2}\left(k_{p}x\right)\), so \(\dd\left(U^{2}\right)/\dd x =-V_{0}^{2}k_{p}\sin\left(2k_{p}x\right)\) and \(u_{s}=-\left(3/8\omega\right)\dd\left(U^{2}\right)/\dd x\) is Equation (A66.34). Take a nodal line at \(x=0\) and the neighbouring antinode at \(x=\pi/2k_{p}\): on the interval between them \(\sin\left(2k_{p}x\right)>0\), so \(u_{s}>0\) and the flow is directed towards the antinode. By the reflection symmetry about the nodal line the same holds on the other side, so the nodal lines are lines of divergence of the slip flow and the antinodes are lines of convergence. Mass conservation then requires the fluid to rise above each antinode and to descend over each node, closing the circulation with an outward branch aloft.

The statement Equation (A66.15) makes about \(\abs{U}\) is general; what is special to the plate is Lemma A66.5, which places the maxima of \(\abs{U}\) over the nodes. The two together are what invert the figure.

Example A66.7 (The scales, in SI).

Take a plate sounding at \(f=500\,\mathrm{Hz}\) with a bending wavelength \(\lambda_{p}=0.10\,\mathrm{m}\), so \(\omega=3.14\times 10^{3}\,/\mathrm{s}\) and \(k_{p}=63\,/\mathrm{m}\), in air of kinematic viscosity \(1.5\times 10^{-5}\,\mathrm{m}^{2}/\mathrm{s}\) and sound speed \(343\,\mathrm{m}/\mathrm{s}\). Then

\begin{equation}\tag{A66.35} \delta=\sqrt{\frac{2\times1.5\times 10^{-5}\,\mathrm{m}^{2}/\mathrm{s}} {3.14\times 10^{3}\,/\mathrm{s}}} =9.8\times 10^{-5}\,\mathrm{m}\approx0.1\,\mathrm{mm}\ec \end{equation}

against an acoustic wavelength \(c/f=0.69\,\mathrm{m}\). The two hypotheses of Lemma A66.5 are met with room to spare in one case and by about a factor of seven in the other: \(k_{p}\delta=6.3\times 10^{-3}\ll1\), and \(k_{p}/\left(\omega/c\right)=63/9.2=6.8\gg1\). The second ratio is the one to watch, since it fails at the coincidence frequency where the bending wave becomes sonic, and above it the plate radiates and the near field is no longer evanescent.

With a plate displacement amplitude \(A_{p}=50\,\mu\mathrm{m}\), so \(V_{0}=\omega A_{p}=0.16\,\mathrm{m}/\mathrm{s}\), Equation (A66.34) gives a peak slip velocity

\begin{equation}\tag{A66.36} \frac{3V_{0}^{2}k_{p}}{8\omega} =\tfrac{3}{8}\,\omega A_{p}^{2}k_{p} =1.9\times 10^{-4}\,\mathrm{m}/\mathrm{s} \approx0.2\,\mathrm{mm}/\mathrm{s}\ec \end{equation}

which moves a grain across a five-centimetre cell in a few minutes — slow, steady and unmistakable, which is what the observation reports. The same amplitude gives a peak plate acceleration \(\omega^{2}A_{p}=4.9\times 10^{2}\,\mathrm{m}/\mathrm{s}^{2}\), some fifty times \(g\), so sand is thrown vigorously; the two mechanisms are operating simultaneously and on different powders, exactly as the chapter says. Rests on Equations (A66.4) and (A66.34).

The same mechanism in Kundt's tube

Corollary A66.8 (Dust ridges at the displacement nodes).

In a gas column carrying a standing wave of wavenumber \(k\) along a tube, the tangential velocity at the wall is \(U(x)=U_{0}\sin\left(kx\right)\) with its maxima at the displacement antinodes. Equation (A66.15) then gives

\begin{equation}\tag{A66.37} u_{s}=-\frac{3U_{0}^{2}k}{8\omega}\sin\left(2kx\right) =-\frac{3U_{0}^{2}}{8c}\sin\left(2kx\right)\ec \end{equation}

directed from each displacement antinode towards the displacement nodes on either side. A powder swept along the wall by that flow therefore accumulates at the displacement nodes, spaced by half a wavelength — which is Phenomenon 39.12. Rests on Theorem A66.3, Equation (A66.15) and Equation (39.17).

Proof.

Derives Corollary A66.8. In a standing wave the velocity amplitude is greatest at the displacement antinodes and zero at the nodes, and the wall is parallel to the axis, so the tangential field imposed on the Stokes layer is \(U_{0}\sin\left(kx\right)\) with \(U_{0}\) the velocity amplitude. Then \(\dd\left(U^{2}\right)/\dd x=U_{0}^{2}k\sin\left(2kx\right)\) and Equation (A66.15) gives Equation (A66.37), the second form using \(\omega=ck\). Between a node at \(x=0\) and the antinode at \(x=\pi/2k\), \(\sin\left(2kx\right)>0\) and \(u_{s}<0\): the flow runs from the antinode back to the node. So the displacement nodes are lines of convergence and the ridges form there.

Phenomenon 39.12 asserts this collection and uses the ridge spacing to measure a wavelength; the chapter takes the location of the ridges from the observation. It is worth noting that the mechanism is the same as the plate's and the apparent reversal between them is not in the streaming at all but in Lemma A66.5: in the tube the maxima of \(\abs{U}\) coincide with the visible antinodes of the wave, whereas over a plate they sit above its nodal lines. In both cases the powder goes where \(\abs{U}\) is least.

What is not derived here

Remark A66.9 (Three gaps, and why they are left open).

Which branch a given grain samples. By Proposition A66.4 the mean flow reverses within the layer, so a grain lying in contact with the plate is not in the same current as one riding above it. A lycopodium spore is some \(30\,\mu\mathrm{m}\) across against the \(\delta\approx0.1\,\mathrm{mm}\) of Equation (A66.35): it protrudes into the layer but does not clear it, so which branch dominates the drag on it is a quantitative question about a body of comparable size to the layer, and neither Theorem A66.3 nor Proposition A66.4 settles it. What is derived here is the outer branch and its direction, which is precisely the bound Remark 39.9 sets.

Adhesion. The competition the chapter names — between the streaming drag and the residual contact friction — requires a model of the grain's adhesion to the plate. There is none in this treatise, so no threshold radius separating the two powders is predicted, and none should be read into Equation (A66.36).

The figure itself. Equation (A66.34) was computed for a one-dimensional mode shape. A real Chladni figure is two-dimensional, and the streaming above it is a two-dimensional pattern of cells whose stagnation structure is not obtained by writing \(\sin\left(2k_{p}x\right)\) twice. That the powder ends up on the antinodal regions follows from the sign of Equation (A66.15) along any line crossing a nodal curve, which is all that is claimed.

Remark A66.10.

Rayleigh Acoustic Streaming Above a Vibrating Surface discharges the derivation owed at Phenomenon 39.8 of Experiment: Waves and Acoustics, in the Chladni experiment Section 39.3. The reader returning there should carry back the reason the chapter keeps the phenomenon at all. The sand figure and the lycopodium figure are traced by the same mode of the same plate at the same amplitude, and they are complementary: one records where the plate is still, the other where the air is still. The first is a threshold in \(\omega^{2}A\) against \(g\), obtained in Continuum Mechanics and Elasticity; the second is Equation (A66.15), a second-order effect in a fluid that the plate merely stirs. Neither figure is the eigenfunction, and an experiment that images a field through a tracer measures the tracer as well as the field — which is the standing warning Experiment: Waves and Acoustics attaches to Phenomenon 39.8, and which this derivation makes quantitative.