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Q f i i c e of NCJ'J~D R e s e a r c h
D e p o r t m e n t of the W a v y
C o n t r a c t N o n r - 2231 2 8)
THEORY OF T H E ACOi iST IC ABSORPTION B Y A GAS BUBBLE IN A LIQUID
Office of Naval Research Department of the Navy Contract Nonr-220(28)
THEORY O F THE ACOUSTIC ABSORPTION
BY A GAS BUBBLE IN A LIQUID
by
Din-Yu Hsieh and Milton S. P lesse t
Reproduction in whole o r in pa r t is permit ted fo r any purpose of the United States Government
Engineering Division California Institute of Technology
Report No. 85-19 November, 1961
THEORY OF THE ACOUSTIC ABSORPTION
BY A GAS BUBBLE IN A LIQUID
by
Din-Yta Hsieh and Milton S. Plesset
Abstract
A complete analysis of acoustic absorption by a spherical gas
bubble i s developed by the application of the classical Rayleigh method.
The absorption considered i s that due to the viscosity and heat conduct-
ion of the gas bubble. Specific results a re presented for the S-wave
scatter and absorption for the case of an air bubble in water, and the
absorption effects of viscosity and heat conduction alone a re calculated
explicitly. The results found here a re of similar magnitude to those
found by Pfriem and Spitzer who used an approximate procedure.
Introduction
While the scattering of sound waves by a spherical gas bubble in a
1 liquid has received extensive treatment by the familiar Rayleigh procedure , a complete analysis of the acoustic absorption does not appear to be avail-
able. This absorption is a consequence of viscosity and heat conduction
2 in the gas bubble. Results for the absorption have been obtained by Pfriem
3 and Spitzer , among others, but these approaches were based on approxi-
mate models which a re limited to the case of spherically symmetric
bubble oscillations. It follows that the scatter and absorption is determined
only for the case in which the S-wave i s significant. It i s found here that
the long wavelength limit of the present analysis is in approximate agree-
ment with the results of previous calculations.
The calculation here will be made first of the absorption due t o the
viscosity of the gas, and then the absorption due to both the viscosity and
the heat conduction of the gas i s determined. It i s shown in this way that
the thermal absorption i s more important than the viscous absorption in
the range of bubble sizes and acoustic frequencies of general interest.
The numerical results which are given below show the scattering and
-absorption cross sections for an air bubble in water with viscosity only
compared with the corresponding cross sections with heat conduction only.
1 See, for example, Lord Rayleigh, IrTheory of Sound, Vol. 11, p. 282, Dover Publications (New York, 1945); V. C. Anderson, J.Acous. Soc.
-3 A m . , &2, 426-431 (1950).
L H. Pfriem, Akustische Zeitschrift, 2, 2.02- 21 2 (1 940). 2 -I
Lo Spitzer, J r . , OSRD Report M05, Sec. 6.1-sr20-918 (1943).
Viscous Absorption
The gas bubble will be taken to have the equilibrium radius - a , and
a spherical coordinate system will be used with origin at the center of the
bubble. The radial distance from the origin i s r and the polar angle be-
tween the radius vector and the z-axis i s It, . The disturbance represent-
ing the sound wave field outside the gas bubble can be described by the
velocity potential, 9 , which satisfies the wave equation
where c i s the sound speed in the liquid. The appropriate solution of W
Eq. ( I ) , in the presence of the gas bubble, will be composed of an
incident plane wave of unit amplitude and of angular frequency o and
scattered waves:
where kw i s the wave number given by kw = w/cw, hc is the spherical
Hankel function of the first kind of order C , Pd is the Legendre poly-
nomial of degree 8 , and the S a re constants to be determined. Using E
the familiar expansion of a plane wave
ikz ikrcos* e = e = iC (24 +l)jC (kr) PC (cos*)
where j i s the spherical Bessel function of order C , one may write E
the su~erposit ion of incident and scattered waves as
The acoustic'velocity field is given by Vy , and the acoustic pressure i s
given by -pway /at. If this pressure i s written in the form
where Pw is the mean, or unperturbed, pressure then
The mean pressure Pw is related to the equilibrium gas pressure Po
as follows:
where tr i s the surface tension constant. In particular, the perturbation
pressure, Pwp, at the bubble wall, r = a , i s given by
P w P = i u p w [ie (28+l)je(kWa)+sChC(kwa)] P 4 (cos$)e - iot , ( 6 )
and the radial component of the velocity a t r = a is
v r = [ ie ( 2 ~ + l ) ~ ~ ( k w a) + se hl(kwa)] kwPe (cos $) e - iwt (7)
Within the gas bubble, the motion of the fluid i s governed by the
equation of continuity
4 ' by the momentum equation
and by the equation of state
In these equations p is the density, Po i s the equilibrium value of the
density, v i s the fluid velocity, q is the coefficient of shear viscosity, *r
p i s the coefficient of bulk viscosity, and y i s the ratio of the specific
heat of the gas at constant pressure to the specific heat a t constant volume.
In Eq. (9) it has been assumed that there a re no body forces, and it has
been assumed further that the coefficients of viscosity a re constants,
Eq. (1 0) states the gas expands and contracts adiabatically. It may also
be remarked that the s t ress on a surface element with outward unit normal
The motion will be taken to be irrotational and then the system of
equations will be linearized. If one writes
4 ~ . Goldstein, "Lectures on Fluid Mechanics", pp. 89-90, Interscience Publishers, Inc. (New York, 1960).
d
5 L. M. Milne- Thomson, "Theoretical Hydrodynamics1', 3rd. ed. , p. 538, MacMillan Co. (New York, 1955).
the linearized. equations obtained by treating r , p, 0 and v as small H
quantities are
and
p = y r (1 0 ' )
Equations (8'), ( 9 ' ) , and (10') lead directly to the relation
where
With the substitution
- iot P = P e
Eq. (1 2) becomes
where
If one defines
then the complex wave number of Eq. (14) may be written as 3
Since p i s finite at r = 0, the general solution of Eq. (1 3) must have the
form
From Eq. (9') one finds for the radial component of the velocity
It follows that a t r = a
where
Equation (11) gives the perturbed radial stress as
which can also be written
where
This perturbed radial stress at r = a may be put in the form
where by Eqs. (15) and (17)
The boundary conditions at r = a a re that the radial component of
the velocity and the radial component of the s t ress be continuous. Eq, (7)
and (1 7) gjve the velocity relation
A f = S k hl(kwa) + iC (24+l) kw jl(kwa) , e e e w
and Eqs. (6) and (20) give the stress relation
These equations determine A4 and St . Solving for the scattering
amplitudes S one gets e
where
and
Since % and f involve spherical Bessel functions with complex argu- C
ments, it is difficult to perform an evaluation of S for the general case. C
Simplifications can be made, however, when the absolute values of these
arguments a re small in comparison with unity in which case the apherical
Bessel functions may be expanded in rapidly converging power series.
For bubble sizes of general interest and for frequencies in the ordinary
acoustic range, both ( k a 1 and 1 kwa( a re small compared with unity and
the expansion procedure may be employed. In this way scattering
amplitudes after some algebraic manipulations a re found to be in the first
approximation
where
The total scattering cross section i s determined by a familiar procedure 6
in terms of the S as follows
and the absorption cross section i s
6 See, for example, P. Me Morse and H. Feshbach, "Methods of Theoretical Physics" Par t 11, p. 1488, McGraw-Hill Book Co. .(New York, -195 3).
For the extinction cross section one has
The scattering and absorption cross sections which are obtained are thus
Some features of these expressions may be pointed out. The
resonance effect in the cross sections is observed with the different resonant
frequencies for the various modes of excitation. It may also be noted that
in the absorption cross section only the bulk viscosity contributes to the
S -wave absorption. There is , of course, no absorption for the P -wave
since in the present approximation the t = 1 disturbance corresponds to
a translatory os~cillation of the whole bubble without change of shape. There
i s , finally, the familiar result that for 1 x 1 FC 1 Q ~ ( O ) and %(o) give
' essentially the entire scattering and absorption cross sections.
Some numerical results have been computed for the case of an air
bubble in water for Po = 1 atm and T = 20°c. The bulk viscosity of a ir
7 has been taken to be given by P = 0 . 5 7 ~ . The results a re shown in
Figs. 1-4.
Viscous and Thermal Absorption
When the effect of heat conduction in the gas i s included, one can
no longer use the adiabatic equation of state. One has instead an energy
equation and and equation of state connecting pressure, density, and
temperature. The gas will be taken here to be a perfect gas so that the
equation of state i s
where M i s the molar weight and R i s the universal gas constant. The
energy equation is 4
where
------- - 7 ~ . S. Sherman, NACA Tech. Note 3298 p. 2l(July, 9 5 5 ) C Truesdell, J . Rat. Mech. and Anal. - 2, p. 649 (1 95 3).
In these equations K i s the coefficient of heat conduction and c i s the v
specific heat a t constant volumo-. The perfect gas equation of state when
' .linearized becomes
where p, 6 , and 0 have been defined in the previous section. The
linearization of Eq. (30) gives
where D = K / P ~ C ~ is the thermal diffusivity. Equations (8') and ( 9 ' ) to-
gether with Equations (31) and (32) lead to
In Eq. (33) ci = (pol Po) ' I2 i s the isothermal sound speed and ca = ( yF a / p o )If2
i s the adiabatic sound speed. Far periodic oscillations
Eq. (33) becomes
where
2 and as before k = u / ~ .
v
Equation (34) may also be written in the form
with
and
Both 0 and vr a re finite at the origin so that one may write the expansion
of 0 in the form
0 = [ACjC(klr) + Be jC(k2r)] PL (COS*) , for r E a . (39)
At r = a one has the boundary conditions, as before, which ensure the
continuity of the radial components s f the s t ress and of the velocity. It is
now necessary to impose an additional boundary condition to d e t e r d n e the
temperature field. This boundary condition will be taken here to be that
the perturbed temperature, TOO, a t the bubble wall i s zero at all times.
That this assumption for the boundary condition i s a good approximation
may be shown by fhe following physical argument. If the thermal conductiv-
ity of the liquid is K~ and the temi>erature gradient in the liquid a t the
bubble boundary i s ( aT/a r)L. and if the corresponding quantities in the
bubble a re denoted by K~ and ( a/ F ) ~ , then the continuity of heat flow at
the interface requires that
One may observe that ordinarily K so that (=/a r ) c c (aT/ar)G. G 4 3 For example, for water K ~ N 5.9 x I0 (c.g. s . ) and K N 2 x 10 (c.g*so).
G
One may now argue that not only is the temperature gradient in the liquid
a small quantity, but in addition i t comes close to i ts constant value at
infinity in a short distance into the liquid from the bubble boundary. The
heat diffusion length in the liquid i s ( D ~ / w ) 'I2 and the heat diffusion length
in the bubble i s ( D ~ I ~ ) " ~ . Here w i s the angular oscillation frequency
and DL, DG a re the thermal diffusivities of the liquid and the g a s , respact-
ively . The diffusion length, ( D ~ / w ) 'I2, over which the temperature varies
1/2 in the liquid i s small compared with the diffusion length in the gas, ( D ~ / W )
This follows since D c C D For the example of water and a i r one has G'
D N 1.4 x ~ O - ~ ( C . ~ . S . ) and DGu 0.2 (c.g.s.) . Thus one may say L
that the temperature gradient in the liquid is small and further the distance
over which this gradient extends i s small. A s a consequence, the varia-
tian in the temperature at the bubble boundary must be small.
By a procedure similar to that followed to obtain Eqs. (1 7) and (30),
one obtains for r = a
and
where, with a = 1 or 2,
The boundary conditions can now be summarized a s follows:
A j ( k a ) t B j ( k a ) = O ; e c 1 e c 2
8 A f ( 1 ) + B f (2) = S k h ' (kwa) + i (28t l ) kwj; (k,a) ; c e t e e w e
iw Pw iwpw 1 A g ( 1 ) + B g (2) = - P S h (k a ) + -
t L 4 8 w i (2c+l)jt(kwa) . e e 0
one finds S a s c - I'F:
Sc - a- C
with
and
The c ross sections a r e thus determined in principle for any w in t e rms of
S by the general fo rml las for the scattering and absorption c ross sections C
already given in the previous section.
Thermal Absorption
One may determine the effect of heat conduction alone in the
scattering and absorption of sound waves, by omitting the cnqtributions of
the viscous t e rms in the general expressions just found. Of interest for
this case a r e the limits of Eqs. (42) and (43) a s k , ks, dnd k becorn3 v b
infinitely large:
2 2 where kl and k2 a r e now given by simplified expressions
with
and
Explicit expressions for the cross sections will be given only for
the case lk a1 1 in which the important contribution is from the W
S-wave alone. It may be observed that in the frequency range of general
interest one has I ka/kt l 2 cc 1, and the following approximations may be
made :
hen, after some manipulations, the cross sections a r e found to be:
and
,
where
] icosh d - cos d) + (sinh d - sind)
2 2 + I 8(y-2-- (cosh d + cos d) - 36(y;1)- (sinh d + sin d)
d (55)
d
N' = (cosh d - cos d) + 3(y-') (s inhd - s ind) , -d (56)
and
n' = 3(Y-1) [ d(sinhd + sind) - 2 (cosh d - cos d) - 3 . (58) d2(coshd - cos d) + 3 (y-l)d (sinhd - sind)
For d e 1, it i s found, approximately, that
and
n' = (kta) 2 73-
while for ed 1 it i s found that
and
It may be remarked that the resonance frequencies as obtained from
(54') and (5411), show a shift from the isothermal limlt to the adiabatic
limit a s the quantity k a increases. As kt i s actually the inverse of the t
diffusion length, this result certainly agrees with what one would expect
f rom physical arguments. Figure 1, 2, 3 and 4 show some numerical
results for the case of an a i r bubble in water. It can be seen that in the
range of frequencies shown the effect of thermal absorption i s appreciably
larger than the effect of viscosity.
Figure 1. The scattering cross section, Qs(H),
and the absorption cross section, Qa(H), take
the bubble heat conduction only into account. The
scattering cross section, Qs (V), and the absorp-
tion cross section, Q (V) take bubble viscosity a
only into account. The bubble radius i s crn.
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