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Oscillations, Waves, and Interactions - GWDG

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188 R. Mettin<br />

constant to M a = 2πρR 3 /3 where the bar indicates a time average [43]. This uncouples<br />

the translational motion from the oscillation <strong>and</strong> introduces a certain error<br />

which is not always negligible [44,45].<br />

The bubble translational motion is counteracted by a viscous drag force. This<br />

force can be found analytically for a spherical bubble <strong>and</strong> stationary low Reynolds<br />

number flow (Re = 2|U|R/ν ≪ 1, ν being the kinematic viscosity). Depending on<br />

the supposed boundary condition at the bubble surface it reads [6,46,47]<br />

Here F (1)<br />

D<br />

F (1)<br />

D<br />

= −4πρνRU or F (2)<br />

D<br />

= −6πρνRU . (6)<br />

is calculated with a zero shear stress boundary condition at the bubble<br />

surface, <strong>and</strong> F (2)<br />

D assumes a zero tangential velocity, i. e., no-slip boundary condition.<br />

While the former case reflects an “ideal” gas-liquid interface, the latter formula is<br />

valid for a “sticky” or “dirty” bubble, equivalent to a solid sphere. Indeed, surface active<br />

contaminants in the liquid may gather at the bubble interface, <strong>and</strong> in many cases<br />

experimental values from rising bubbles in non-clean liquids tend to yield F (1)<br />

D [46].<br />

If faster bubble translations are considered, the high Reynolds number limit may be<br />

encountered, if the bubble is small enough to be still spherical <strong>and</strong> not deformed (in<br />

water up to Re ≈ 800 [46]). In this situation the “clean” bubble boundary condition<br />

yields [46,47]<br />

F (3)<br />

D<br />

= −12πρνRU , (7)<br />

<strong>and</strong> the “dirty” bubble case results in additional drag proportional to U 2 [46].<br />

For oscillating bubbles, the drag becomes time dependent, <strong>and</strong> analysis gets more<br />

complicated. Some limiting cases are derived in Ref. [48]. In particular, the limit of<br />

high Re or high ( ˙ R/U)Re yields for an ideal (clean) bubble interface again F (3)<br />

D , but<br />

with the substitution of the constants R <strong>and</strong> U by their time-dependent counterparts<br />

R(t) <strong>and</strong> U(t). Measurements of bubble motion in ultrasonic st<strong>and</strong>ing waves<br />

at smaller Re, but higher ( ˙ R/U)Re support this result [10,49]. However, more experimental<br />

investigations, in particular in strong fields, should be undertaken to verify<br />

the theoretical approaches.<br />

5 Bubble life cycles<br />

If we combine all discussed aspects of single bubble dynamics, we can consider the<br />

“life” of a bubble in a given liquid <strong>and</strong> sound field. We restrict our viewpoint to<br />

translation <strong>and</strong> gas diffusion, both supposed to happen on a slower time scale than<br />

the volume oscillation. In a st<strong>and</strong>ing wave, the fate of a bubble is determined by its<br />

initial size R0 <strong>and</strong> position in space x, or, equivalently, the sound pressure amplitude<br />

pa(x) at the initial position. Its life cycle can be represented by a trajectory in the<br />

plane of R0 <strong>and</strong> pa. Main features can be seen if characteristic lines are drawn in that<br />

plane: the threshold of spherical shape instability (SI), the inversion of the primary<br />

Bjerknes force (BJ), <strong>and</strong> the rectified diffusion threshold (RD). Examples of such<br />

diagrams are shown in Fig. 13.<br />

The general direction of a bubble trajectory in this parameter space is towards the<br />

right above the RD line, <strong>and</strong> towards the top below the BJ line. The space above

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