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J Appl Physiol 82: 2045-2053, 1997;
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Journal of Applied Physiology
Vol. 82, No. 6, pp. 2045-2053, June 1997
GAS EXCHANGE, MECHANICS, AND AIRWAYS

MODELING IN PHYSIOLOGY

Stabilized bubbles in the body: pressure-radius relationships and the limits to stabilization

Hugh D. Van Liew and Soumya Raychaudhuri

Department of Physiology, University at Buffalo, State University of New York, Buffalo, New York 14214

ABSTRACT
INTRODUCTION
THEORY AND METHODS
RESULTS AND DISCUSSION
APPENDIX
ACKNOWLEDGEMENTS
FOOTNOTES
REFERENCES


ABSTRACT

Van Liew, Hugh D., and Soumya Raychaudhuri. Stabilized bubbles in the body: pressure-radius relationships and the limits to stabilization. J. Appl. Physiol. 82(6): 2045-2053, 1997.---We previously outlined the fundamental principles that govern behavior of stabilized bubbles, such as the microbubbles being put forward as ultrasound contrast agents. Our present goals are to develop the idea that there are limits to the stabilization and to provide a conceptual framework for comparison of bubbles stabilized by different mechanisms. Gases diffuse in or out of stabilized bubbles in a limited and reversible manner in response to changes in the environment, but strong growth influences will cause the bubbles to cross a threshold into uncontrolled growth. Also, bubbles stabilized by mechanical structures will be destroyed if outside influences bring them below a critical small size. The in vivo behavior of different kinds of stabilized bubbles can be compared by using plots of bubble radius as a function of forces that affect diffusion of gases in or out of the bubble. The two ends of the plot are the limits for unstabilized growth and destruction; these and the curve's slope predict the bubble's practical usefulness for ultrasonic imaging or O2 carriage to tissues.

bubble nuclei; cavitation; decompression sickness; surfactants; surface-active films; ultrasonic imaging


INTRODUCTION

THERE ARE SEVERAL REASONS for interest in the behavior of small, stabilized gas cavities (bubbles) inside the human body. Microbubbles are being developed for enhancement of ultrasonic contrast of blood vessels and other body structures (5, 9, 13, 19, 20, 22, 30, 31). Some of these bubbles are small enough to traverse capillary beds and are stabilized by mechanisms that cause them to persist much longer than a simple bubble of air (23). Also, if microbubbles are permeable to gases, they could carry appreciable amounts of O2 from lungs to tissues; it has been proposed that microbubbles could serve as a substitute for blood hemoglobin (4, 24). Furthermore, if stabilized bubbles are analogs of the micronuclei that may be the precursors of decompression sickness bubbles (18, 34) and the initiation sites for damaging cavitation in an ultrasonic field (2), their behavior is of interest in diving safety and medical uses of ultrasound. In all these cases, the way that the stabilized microbubbles respond to environmental changes is extremely important. If the change causes the microbubbles to become unstabilized, they can cease to exist or can grow into large, damaging bubbles.

Because pressure due to surface tension is a function of bubble size, it is obligatory for the stabilization mechanism to be a function of size as well (23). Two general classes of mechanisms can stabilize bubbles. First, slowly permeating gases (13) remain for relatively long times in the bubbles, while other more rapidly permeating gases diffuse in or out according to their concentrations in the environment (22, 23); total pressure inside is greater than that outside because of pressure due to surface tension. Second, structures at the gas-liquid interface can serve as stabilizers; examples are surface-active films (30), surface-active protein that may be denatured (19, 31), and gelatin (5). We have shown that, despite the differences between the two classes of stabilizing mechanisms, slowly permeating gases and structural stabilizers can be characterized by similar mathematical expressions (23).

The specific objectives of the present paper are to provide two extensions to our previously published theoretical treatments (4, 22-24): 1) to include the idea that there are upper and lower size limits to stabilized bubbles and 2) to consider how bubbles stabilized by various mechanisms can be compared. The crucial aspect of a structural stabilizer is that it must produce a negative pressure inside the bubble to counter the tendency for outward diffusion of the gases inside, especially to counter the strong positive internal pressure due to surface tension when bubbles are small. The theory presented below, couched in a mathematical framework, encompasses this fact and other basic facts that are valid for any stabilized bubble. We present examples to show how bubbles stabilized by different kinds of mechanisms may behave.


THEORY AND METHODS

In recent publications (4, 22-24), prediction of the behavior of stabilized microbubbles in blood depended on an important basic assumption: that the size of stabilized bubbles can vary in response to changes in the bubbles' surroundings; stabilization does not imply a fixed size or rigid structure. This assumption is supported by the observation that the ultrasonic signal from a bubble stabilized by an albumin coating decreased when pressure was applied and then returned to the initial level when pressure was released (15). For present purposes, we add another assumption: that the stabilizing mechanism may fail at some small size or rupture due to overexpansion. For most examples, we drew inspiration from surface films or surfactant monolayers, a specific type of structural stabilizer. Other structural stabilizers will be analogous to surface films in that they counter surface tension but may differ in particulars.

An important related assumption is that the stabilized bubbles are permeable to diffusion of gases, so that diffusive exchanges will occur when there are gas partial pressure differences between inside and outside. The concept that gases diffuse in or out to change the contained volume when stabilized bubbles vary in size contrasts with the idea put forward by Yount and co-workers (32) that stabilized bubbles become impermeable when they are very small. It seems unlikely that a single layer of molecules, particularly if they are largely lipid in makeup, could prevent gas diffusion, even if densely packed. A monolayer could conceivably block water diffusion into the bubble and may slow permeation of some gases (3), but gases with high lipid solubility would have their diffusion enhanced by a lipid monolayer. Stabilized bubbles with multiple layers have been described (20), but if the layers are mainly lipid, permeability may not be appreciably affected.

We take advantage of a simplifying assumption so that we can use radius to characterize size: that stabilized bubbles always remain spherical. This is probably not valid for at least some kinds of bubbles; e.g., bubbles stabilized by shells of denatured protein are said to change shape when small (7), and bubbles stabilized by surfactant have been observed to become nonspherical when the surfactant molecules are forced close to each other (10). The assumption of sphericity and other simplifications mean that the results of our calculations are approximate; this does not detract from our goal of exploring the basic characteristics of stabilized bubbles.

The partial pressures of gases inside a bubble are influenced by hydrostatic pressures (23). The well-known Laplace-Young equation gives the hydrostatic pressure (P) exerted by surface tension on the contents of a spherical bubble
P&ggr; = <FR><NU>2&ggr;</NU><DE><IT>R</IT></DE></FR> (1)
where R is bubble radius.

Glossary

 beta      Exponent defined by Eq. 2, dimensionless
 Delta Pabs Pressure difference for bubble absorption, kPa
 gamma      Surface tension, 50 dyn/cm = 50 kPa · µm
 pi      Constant, ~3.1416
 Pi      Reduction of surface tension due to a surface-active film, dyn/cm
A     Area per stabilizer element on a bubble surface, µm2
Ac     Minimal area per structural element before crushing occurs, µm2
Ao     Actual area that a stabilizer element occupies on a bubble surface, µm2
b     Constant, 2 pi  k T/Ac, kPa · µm
c     Scaling constant for pressure exerted by an elastic sphere, kPa/µm
C&Ggr;     Constant that relates P&Ggr; to a function of bubble radius; units depend on the function
k     Boltzmann's constant, 1.3805 × 10-23 J/°K
n     Number of structural elements in a mechanical stabilizer
Pgamma      Pressure generated by surface tension on a bubble, kPa
P&Ggr;     Pressure generated by a bubble stabilizer, kPa
Pz     Sum of all hydrostatic pressures and partial pressures that could affect diffusive exchanges of a bubble, other than those that depend on bubble radius, kPa
Pzc     Pressure at the crushing radius R*c, kPa
Pzg     Pressure at the critical growth radius R*g, kPa
R     Bubble radius, µm
R'     Unstressed radius of an elastic sphere, µm
R*     Stable radius of a bubble, µm
R*c     Crushing radius of a bubble, µm
R*g     Critical growth radius of a bubble, µm
Ro     Asymptotic minimal radius of a bubble, µm
R*u     Stable radius of bubble when Pz = 0, µm
T     Temperature, °K

A stabilization mechanism exerts a counterpressure (P&Ggr;) against the tendency of surface tension and other forces to cause outward diffusion of the bubble's gaseous contents. A major point for this paper is that the behavior of a bubble is determined by behavior of P&Ggr; as a function of radius; each different stabilizer will have its own P&Ggr; function. To provide examples that have a quantitative basis, we relied on previous theory about bubbles stabilized by an ideal surfactant (23) for our starting point. We needed an expression that can account for the quantitatively different responses to stress that may occur with different kinds of stabilizing structures. We devised Eq. 2 to satisfy this need; APPENDIX A shows the relation of Eq. 2 to ideal surfactant films and bubbles of slowly permeating gas.
P<SUB>&Ggr;</SUB> = <FR><NU><IT>C</IT><SUB>&Ggr;</SUB></NU><DE><IT>R</IT><SUP>(&bgr;+1)</SUP>(<IT>R</IT><SUP>2</SUP> − <IT>R</IT><SUP>2</SUP><SUB>o</SUB>)</DE></FR> (2)
According to Eq. 2, the pressure exerted by the stabilization mechanism is a ratio having a constant in the numerator and radius in the denominator, similar to the Laplace-Young equation, except that P&Ggr; involves the reciprocal of a function of radius instead of the simple reciprocal of radius. If the stabilizer is a surface-active film, the C&Ggr; constant is proportional to the number of molecules in the film. The Ro represents the minimal radius of the sphere made up of the aggregate of the elements of the mechanical stabilizer, and (beta  + 1) is an arbitrary exponent. If beta  and Ro are both zero, Eq. 2 is the formula for a simple, ideal "gaseous" surface-active film (23). Our introduction of the hypothetical beta  and Ro parameters allows us to anticipate the behaviors of real, nonideal surfactants that may be found in nature. Because the function of the stabilizer is to counter surface tension, the value of the right side of Eq. 2 must be >2gamma /R when R is small; it follows that the value of beta  for a stabilized bubble can be any number more positive than -2.0. Our examples using Eq. 2 are intended to portray some possibilities for real stabilizers; the purpose of the examples is to explore the general properties of different possible stabilizer mechanisms.

The hydrostatic pressures and partial pressures that affect the diffusive exchanges of a bubble can be categorized as positive absorptive pressures (Delta Pabs) that give a tendency for shrinkage or as negative absorptive pressures that give a tendency for growth. The sum of all pressures that relate to Delta Pabs is
&Dgr;Pabs = P<SUB>&ggr;</SUB> − P<SUB>&Ggr;</SUB> + P<SUB>z</SUB> (3)
All terms in Eq. 3 are in units of kPa (1 atm abs = 101.3 kPa); they are hydrostatic pressures or partial pressures. The Pgamma and P&Ggr; terms are functions of bubble size, as seen by Eqs. 1 and 2. The term Pz symbolizes the sum of all influences that are independent of bubble size. Blood pressure is an example of a positive absorptive hydrostatic Pz. Another type of positive Pz is the gas concentration difference due to the inherent unsaturation caused by O2 metabolism, the so-called O2 window (25), for a bubble in tissue or venous blood. The gas supersaturation that occurs in tissues of a diver who ascends from depth (27) is an example of a negative, size-independent concentration difference; the dissolved gas in the tissue is temporarily supersaturated, relative to the ambient pressure, so it tends to diffuse into a bubble.

Computations and plotting. We provide graphic examples developed using Microsoft QuickBasic on a Macintosh Classic computer. The plots assume surface tension to be 50 dyn/cm, a value reported for surface tension of blood (29).


RESULTS AND DISCUSSION

The three panels of Fig. 1 illustrate the effects of changes in Pz for one particular bubble. Figure 1A is the fundamental balance-of-forces diagram introduced in another publication (23). The uppermost dashed trace shows the absorptive pressure due to surface tension as a function of bubble radius. If unopposed, surface tension would have little effect when radius is large and, at small radii, would greatly elevate the hydrostatic pressure inside, causing outward diffusion of all constituent gases. The lowermost dashed trace in Fig. 1A shows P&Ggr;, the growth pressure exerted by a stabilization mechanism; if it were unopposed, the stabilizer would produce a growth tendency of about -50 kPa when radius is 2 µm and would exert very strong growth pressures at smaller radii.


Fig. 1. Fundamentals of pressure difference for bubble absorption: (Delta Pabs)-vs.-radius plots for 1 particular stabilized bubble. Dashed curves of pressure generated by surface tension on a bubble (Pgamma ) and pressure generated by a bubble stabilizer (P&Ggr;) are the same in A-C (Pgamma curve drawn from Eq. 1, P&Ggr; curve from Eq. 2 for C&Ggr; = 400 kPa · µm3 with beta  = 0 and Ro = 0). A: curve labeled Sum (from Eq. 3) is the resultant of 2 oppositely acting pressures caused by surface tension and by stabilizer. open circle , Stable radius; bullet , point where stabilization mechanism fails; square , maximum of Sum curve. B: addition of a size-independent absorptive influence (horizontal dashed trace) moves Sum curve upward from where it was in A and decreases stable radius. C: 3 different Sum curves correspond to different Pz values (dashed horizontal line segments). star , "Critical growth" point where, because of a Pz of -20 kPa, bubble is on the verge of growing irreversibly. See Glossary for other definitions.
[View Larger Version of this Image (16K GIF file)]

The radius is stable where the Sum curve, the resultant of Pgamma and P&Ggr; influences, crosses the axis for zero Delta Pabs in Fig. 1A (at 2 µm). At the crossing, there is a positive slope so that if the bubble were slightly larger than its stable size, pressure due to surface tension would be greater than the negative pressure due to the stabilizer; there would be a positive pressure inside the bubble, which would cause gas inside to diffuse out until the bubble had shrunk down to the stable size. Conversely, if radius were between 1.5 and 2 µm in Fig. 1A, the bubble would grow to the stable radius. Every stabilized bubble, no matter what the mechanism, must have a positive slope on a balance-of-forces diagram, such as that illustrated in Fig. 1A. Stabilization requires that the P&Ggr; must be larger in magnitude than Pgamma when radius is small. Within that constraint, P&Ggr; curves can have different shapes, as discussed below.

In addition to the point where the Sum curve crosses the axis for zero Delta Pabs, two other important features in Fig. 1A are the point at which the Sum curve reaches a maximum (the square, which will be discussed just below in connection with Fig. 1C) and the left-hand end of the P&Ggr; curve. The bullet  represents the minimum size for the bubble's stabilization; we arbitrarily assign a minimum radius of 1.5 µm for this particular bubble; at smaller radii, the Sum curve does not exist because of failure of the stabilization mechanism. This is discussed further, in connection with Fig. 2A.


Fig. 2. Stability range for particular bubble that was shown in Fig. 1A. Solid traces show Sum curves for limiting possibilities. black-lozenge , crushing radius; note that it is directly above bullet  on P&Ggr; curve; star , critical growth radius. Inset: counterclockwise rotation of either of solid curves of panel A gives a plot of radius vs. pressure. B: information from panel A replotted on a radius-vs.-Pz plot, with added points for unstressed radius (triangle ) and for a bubble in venous blood (x).
[View Larger Version of this Image (15K GIF file)]

Figure 1B shows the effect of adding a third pressure, a Pz of +30 kPa (arrow), to the Pgamma and P&Ggr; pressures of Fig. 1A. The addition moves the Sum curve up by 30 kPa over the entire range of radii. Comparison with Fig. 1A shows that the point where the Sum curve crosses the axis has moved to the left by ~0.3 µm. If a negative Pz had been added, the Sum curve would have been lowered instead of raised. Adding or subtracting various Pz values simply translates the Sum curve up or down, and the square  at the maximum of the Sum curve will be at the same radius, no matter what the Pz. It is shown next that when the maximum of the Sum curve is brought below the axis for zero Delta Pabs, the bubble cannot be stable; it grows irreversibly.

Irreversible growth. The three solid Sum curves on Fig. 1C show effects of three different Pz values. A negative Pz acts in the same direction as the stabilization mechanism; both tend to cause growth. When Pz is negative enough to bring the maximum of the Sum curve below the axis for zero Delta Pabs, a previously stabilized bubble grows into a relatively large, unstabilized bubble that can do damage in the body, as in decompression sickness (21, 27). For the curve with Pz of -45 kPa in Fig. 1C, there is no stable radius so the bubble grows irreversibly at all radii. The stabilized bubble with Pz of -20 kPa has a unique point (star ); Pz for that point is the critical Pz for irreversible growth, Pzg. When a bubble is located at that point, the bubble would grow if, by chance, Pz became a little more negative or the radius increased a little. When the critical growth pressure is exceeded, the rate of growth that occurs increases as size increases because of the negative slope of the Sum curve to the right of the curve's maximum. As outlined before (21), when a small bubble is in an environment that fosters growth, there is a positive-feedback loop, whereby increased radius due to growth causes decrease of pressure due to surface tension, which encourages further growth. There is also a positive-feedback loop involving surface area of the bubble; as gases diffuse into the bubble, surface area increases, which, in turn, increases the amount diffusing under a particular gas concentration gradient.

Crushing. A bubble stabilized by a mechanical structure can be expected to behave in a discontinuous manner at small radii; a strong positive Pz may cause the bubble to reach its minimum size, beyond which it changes drastically or ceases to exist. Items in support of this possibility are the idea that micronuclei, the putative precursors of decompression-sickness bubbles, can be inactivated or "crushed" by high pressure (26); observations of "buckling" or "crumbling" of surface-active films (Ref. 1, p. 115; Ref. 17); observations of fissioning of bubbles into several smaller bubbles (33); and irreversible loss of ultrasonic signal from several types of microbubble contrast agents when pressure is applied to them (28).

The bullet  in Fig. 1A showed the radius and pressure combination at which the bubble's stabilization mechanism fails. We envision that there will be failure of the stabilizing molecules in most kinds of mechanical structures; we call the limiting small size the "critical crushing" radius. A Pz of +50 kPa will bring the Sum curve of the bubble depicted in Fig. 1 to 1.5 µm, the critical radius for bubble destruction or crushing; this is illustrated by the top solid curve in Fig. 2A.

When there is no longer a stabilization mechanism because of crushing, we envision that the bubble's gas contents rapidly diffuse out under the influence of surface tension. Hyldegaard et al. (12) observed that once a bubble in animal tissues had disappeared, application of growth influences did not make it reappear. On the other hand, Liebermann (14) observed that a residue left after apparent disappearance of free, unstabilized bubbles in water gave rise to new bubbles if the liquid was decompressed; this suggests that some sort of stabilized micronuclei remained in the residue. Bubbles stabilized by slowly permeating gas (13) may be an exception to the idea that all bubbles can be crushed; if the gas does not change phase to a liquid, such bubbles would not be expected to fail cataclysmically but will be absorbed more rapidly when Pz is large.

Limits to stabilization. A Pz of -20 kPa brought the Sum curve for the particular bubble shown in Figs. 1 and 2 to one limit of stability, where the bubble would grow irreversibly (lower solid curve in Fig. 2A) and addition of a sufficiently large positive Pz (+50 kPa) moved the Sum curve up to the critical point where crushing would occur (top solid curve in Fig. 2A). The Sum curves for all possible stabilized sizes must lie between the two solid curves shown in Fig. 2A. Because the two curves in Fig. 2A are for the same bubble, which has a particular C&Ggr;, they are identical except that they are translated vertically from each other by differences in Pz. The inset shows either of the two solid Sum curves of Fig. 2A rotated 90° counterclockwise. Such a pressure-vs.-radius display is analogous to stress-vs.-strain diagrams for other materials. The display is made practical by using Pz for the pressure axis, as we have done in Fig. 2B.

Radius vs. Pz. Figure 2B shows all possible radius-vs.-Pz combinations for the particular bubble under consideration when it is in a stable condition. When Pz is zero, the radius is unstressed (at radius = 2 µm). When stress due to Pz is positive, radius declines with increasing Pz until the bubble reaches the positive pressure that causes crushing (at radius = 1.5 µm). When stress due to Pz is negative, radius enlarges until the bubble reaches the negative pressure that causes unstabilized growth (at radius = 3.4 µm). Compliance of the bubble can be defined as the slope of the radius-vs.-Pz curve. Clearly, compliance is specific to the prevailing Pz. The changes of radius in Fig. 2B correspond to large changes of volume because of the cubic relation between radius and volume: the volume at the critical growth radius is 12 times greater than the volume at the critical crushing radius. APPENDIX B presents the mathematical relationships implicit in the type of curve shown in Fig. 2B for one particular kind of structural stabilizer.

In traversing the circulatory system, a stabilized bubble will encounter various Pz values (23). In mixed venous blood, the sum of partial pressures of dissolved gases is less than atmospheric pressure because of removal of O2 by metabolism. In an air-breathing subject, the value of this inherent unsaturation is ~7 kPa (25); the corresponding point on Fig. 2B is shown by x. In O2 breathing, the inherent unsaturation is much higher, such as 89 kPa (24); this falls beyond the black-lozenge  on the curve in Fig. 2B. If subjected to Pz of 89 kPa, the particular bubble illustrated here would be crushed in the tissue capillaries or venous blood. To have persistent bubbles that can recirculate in a person breathing pure O2, it would be necessary to have a bubble that is stabilized by a mechanism with a stronger resistance to crushing.

Note that because displays such as Fig. 2B are for the condition of stability, the bubble is in diffusive equilibrium with its surroundings for all points on the curve. After a rapid change in the environment, there will be a transient phase in which the bubble leaves the radius-vs.-Pz curve. Diffusive readjustment of contents will bring the bubble back to rest on the curve.

Varieties of stabilizers. Figures 1 and 2 show how a single bubble with a particular stabilization mechanism behaves as environmental conditions change. In what follows, we focus on distinguishing between different stabilization mechanisms. We hope to gain insights into possibilities for various kinds of real bubbles by simulating the behaviors of hypothetical bubbles having various characteristics; to do so, we vary the parameters in Eq. 2.

Figure 3A, drawn for the specific kind of stabilizer that is dealt with in APPENDIX B, shows that larger C&Ggr; moves the stabilizer curve to the right and down. Figure 3B shows that larger C&Ggr; gives larger bubbles that require less negative Pz for unstabilized growth and less positive Pz for crushing; in Fig. 3B, larger bubbles are more fragile than small bubbles: they are less resistant both to growth and to crushing. Higher C&Ggr; gives a steeper slope at Pz = 0. 
Fig. 3. Consequences of variations of constant relating P&Ggr; to a function of bubble radius (C&Ggr;); dashed curves were drawn from Eq. 2 with beta  = 0 and Ro = 0. A: location of stabilizer curves for different values of C&Ggr;. bullet , Crush points for an arbitrary choice of 140 kPa · µm for b in Eq. B11. B: radius-vs.-Pz curves for the 3 cases of panel A. See Glossary for other definitions.
[View Larger Version of this Image (14K GIF file)]

The nature of the stabilization mechanism determines the shape of a curve of stabilizer pressure as a function of bubble size. Our examples so far have used Eq. 2 with a (beta  +1) exponent of 1.0 and Ro asymptote of zero; these choices approximate the behavior of a bubble stabilized by either a slowly permeating gas or by a "gaseous" type of surfactant film (23). We presume that we can approximate curves for other types of surfactants or mechanical structures by varying the beta  exponent or the Ro asymptote; a few examples are presented in Fig. 4.
Fig. 4. Variations of characteristics of structural stabilizers. As in Fig. 3, stabilizer curves are at left, radii as a function of Pz are at right. A and B: variation of exponent beta  in Eq. 2 (with C&Ggr; = 400 kPa · µm3, Ro = 0; crushing arbitrarily set at Pz = 23.4 kPa). C and D: variation of Ro in Eq. 2 [with C&Ggr; = 400, beta  = 0, crushing occurs when (Rc*2 - R2o) is less than a certain value, arbitrarily set at 1.5 µm2]. See Glossary for other definitions.
[View Larger Version of this Image (24K GIF file)]

Figure 4, A and B, displays effects of alterations in the value of the beta  parameter to simulate variations in the mechanical properties of stabilizers. When beta  is large, the P&Ggr; curves are steeper (Fig. 4A), the radius-vs.-Pz curves are more horizontal where they cross the axis for zero Pz (Fig. 4B), and the bubbles are more resistant to unstabilized growth (star  in Fig. 4B). We cannot anticipate the effect of different beta  values on the crushing phenomenon, so we arbitrarily chose to set the crushing point at a constant Pzc. However, it may be that the steeper curves in Fig. 4A are also more resistant to crushing; if so, the curves for larger beta  values should have the crush point at greater negative Delta Pabs in Fig. 4A and greater positive Pz in Fig. 4B.

Because Ro characterizes the aggregate surface area of elements of the mechanical stabilizer, larger Ro indicates larger elements. An increase in Ro moves the asymptotes to the right and causes divergence of the stabilizer curves from each other at negative Delta Pabs values (Fig. 4C). The consequences are that there is little variation of the Pz for unstabilized growth but there is variation in the crushing Pz (Fig. 4D). Bubbles with large Ro are less resistant to crushing.

Note that the kinds of diagrams shown in Figs. 3 and 4 may be crude approximations for real bubbles. The P&Ggr; curves may not fall smoothly to the left as shown in Figs. 3A, 4A, and 4C if there are changes in the state of the material in the structure. For example, if a surfactant film goes from "gaseous" to "liquid" to "solid" states (Ref. 1, p. 129-133), each state may have its own smooth curve, which is joined to the curve for the next state at a transition point. Other complexities are likely. For example, a bubble that collapses like a football bladder when its volume decreases would have different radii in different aspects, and one of the radii would change much more than others when volume decreases.

Coherent elements. Some bubbles may be stabilized by elements or molecules that tend to cohere to each other, such as denatured proteins (7, 15, 19, 28, 31). Such materials can be expected to exhibit the property of elasticity, which would result in a Delta Pabs-vs.-radius plot that rises without leveling off, as depicted in Fig. 5A. As in Figs. 1, 2, 3, 4, the Sum curve is the sum of contributions from the Pgamma curve and the P&Ggr; curve. For this case, the P&Ggr; curve was drawn by a formula inspired by properties of elastic sheets: P&Ggr; = c [R - (R'2/R)]. This formula incorporates the idea that force per unit length exerted by an elastic sheet that covers a sphere is proportional to change of area from an unstressed area (with radius = R') and was derived by analogy with Eqs. A1-A6 in APPENDIX A. For Fig. 5, we arbitrarily assigned the scaling constant c to be 10 kPa/µm and R' to be 4 µm. Although the Sum curve has no maximum, irreversible growth can occur by a different mechanism. The discontinuity on the right end of the P&Ggr; curve of the elastic, coherent material in Fig. 5A represents failure of the stabilizer because of excessive stretch, analogous to explosion of a balloon when it is overinflated. In Fig. 5B, an added Pz of -50 kPa lowers every point on the Sum curve so that the stable radius is at the point of the discontinuity in the stabilizer curve. After the stabilization structure ruptures and no longer provides a counterpressure, there are only two forces acting on the gases in the bubble: surface tension is small because the size of the bubble is large, and the negative Pz that was used to induce the present state is relatively large. The sum of these puts the bubble in the growth region, so it grows (arrow in Fig. 5C).
Fig. 5. Behavior of a bubble stabilized by an elastic material. A: Sum curve proceeds upward in absorptive region at right without a maximum. open circle , Stable radius. Stabilization may fail due to crushing (left bullet ) or overexpansion (right bullet ). B: addition of a large negative Pz lowers the sum curve and increases stable radius to where it is overstretched and destroyed (black-lozenge ). C: after stabilizer disappears, bubble grows irreversibly (arrow). D: Pz-vs.-radius plot of bubble shown on panels A-C. triangle , Unstressed radius; black-lozenge , rupture points; compliance is more uniform over range of Pz than with Figs. 3 and 4.
[View Larger Version of this Image (24K GIF file)]

Figure 5D is a plot of radius as a function of Pz for the elastic stabilizer, analogous to Fig. 2B. The black-lozenge  on the left represents the point at which the structure ruptures, producing an unstabilized bubble that grows. We envision that this sort of elastic membrane will crush or rupture at high positive pressures in the same way as a surfactant-stabilized bubble, so that it ceases to serve as a stabilizer at some small radius (black-lozenge  on right).

Applications of radius-vs.-Pz curves. Knowledge of how bubbles behave when they are stabilized by a particular mechanism would allow practitioners to choose the bubble with appropriate characteristics for a particular purpose. Also, specific characteristics can be sought in the formulation of bubbles by new techniques or by the use of new materials. It might be desirable, for example, to have bubbles that would not be crushed at all under physiological conditions or, alternatively, an application might call for bubbles that would be crushed by arterial blood pressure. A radius-vs.-Pz curve conveniently summarizes the characteristics of different kinds of stabilized bubbles; the critical growth radius, the unstressed radius, the crushing radius, and the bubble's compliance all appear on one simple graph. Data to characterize a particular bubble on a radius-vs.-Pz curve could be obtained by microscopic observations of it during slow changes of external pressure while dissolved gases in the liquid environment are controlled.

We next cite three cases where distinguishing between different types of bubbles may be desirable. First, if bubbles are used to augment O2 carriage by blood (4), the amount of O2 that is unloaded at a particular partial pressure depends heavily on the bubble's tendency to change size as well as on the local PO2 (24). Therefore, a highly compliant bubble is desirable if one wants to unload large amounts of O2 in tissue at a given partial pressure. The curves in Fig. 3B indicate that bubbles with larger C&Ggr; generally exhibit greater compliance (change of radius per change of pressure). In contrast, noncompliant bubbles, such as those with higher beta  exponent illustrated in Figs. 4A and 4B, would be less effective in O2 delivery.

Second, it remains to be seen which stabilizer characteristics give the best signal when bubbles are used for ultrasonic contrast (16, 35): large elements, many elements, or large compliance. In some circumstances, the ultrasonic signal due to a bubble is proportional to the sixth power of radius (35), so stabilizing mechanisms that give rise to large bubbles offer far more enhancement of a given signal than mechanisms that make for smaller bubbles.

The third case concerns the idea that the precursors of decompression-sickness bubbles are permanent or semipermanent small bubbles or gaseous "micronuclei" (11, 21, 34) stabilized by structures of the kind discussed in this paper. If so, Eqs. B8 and B11 indicate that large micronuclei are both more easily destroyed by crushing and more easily transformed into bubbles. Exposure of a diver to high environmental pressure is thought to crush micronuclei (26). If so, the crushing would delete some of the population of micronuclei, so there would be fewer available to be forced into irreversible growth to cause damaging bubbles by the subsequent decompression (18). Furthermore, it would be desirable to determine the characteristics of the stabilizing mechanisms of decompression-sickness precursors; perhaps it will be possible to develop techniques to interfere with their transformation into damaging bubbles.


ACKNOWLEDGEMENTS

We are greatly indebted to Mark E. Burkard for insightful suggestions and criticisms.


FOOTNOTES

Address for reprint requests: H. D. Van Liew, Dept. of Physiology, 25 Sherman Annex, State Univ. of New York at Buffalo, SUNY, Buffalo, NY 14214.

Received 3 May 1996; accepted in final form 11 February 1997.


APPENDIX A

Relationship of Eq. 2 to Surface Films

Equation A1 describes the behavior of various nonideal gaseous surfactants on a planar surface, such as on a Langmuir trough (Ref. 6, p. 228)
&Pgr;(<IT>A</IT> − <IT>A</IT><SUB>o</SUB>) = <IT>nk</IT>T (A1)
Total area A that is occupied by the surface-active film has a minimum, Ao, and the reduction of surface tension due to the film, Pi , is related to the number n of molecules or elements in the film. Because Pi  is the difference of surface tension between pure solvent and solvent containing the surfactant (Ref. 6, p. 218), it has the nature of a surface tension, so the Laplace-Young equation can characterize the counterpressure on a spherical bubble due to the surfactant
P<SUB>&Ggr;</SUB> = <FR><NU>2&Pgr;</NU><DE><IT>R</IT></DE></FR> (A2)
Substitution with Eq. A1 gives
P<SUB>&Ggr;</SUB> = <FR><NU>2<IT>nk</IT>T</NU><DE><IT>R</IT>(<IT>A</IT> − <IT>A</IT><SUB>o</SUB>)</DE></FR> (A3)
Converting the area terms to radius terms yields
P<SUB>&Ggr;</SUB> = <FR><NU>2<IT>nk</IT>T</NU><DE>4&pgr;<IT>R</IT>(<IT>R</IT><SUP>2</SUP> − <IT>R</IT><SUP>2</SUP><SUB>o</SUB>)</DE></FR> (A4)
where R is the radius of the bubble, and Ro is the minimal radius.

We group constants in Eq. A4 into a single constant C&Ggr;
<IT>C</IT><SUB>&Ggr;</SUB> = <FR><NU><IT>nk</IT>T</NU><DE>2&pgr;</DE></FR> (A5)
Thus the C&Ggr; constant is proportional to the number of stabilizer elements in the interface (23).

Substitution of the C&Ggr; constant into Eq. A4 yields
P<SUB>&Ggr;</SUB> = <FR><NU><IT>C</IT><SUB>&Ggr;</SUB></NU><DE><IT>R</IT>(<IT>R</IT><SUP>2</SUP> − <IT>R</IT><SUP>2</SUP><SUB>o</SUB>)</DE></FR> (A6)
To allow approximation of some types of stabilizers that differ in properties from the film characterized by Eq. A1, we broaden Eq. A6 by arbitrarily raising one of the R terms to a power
P<SUB>&Ggr;</SUB> = <FR><NU><IT>C</IT><SUB>&Ggr;</SUB></NU><DE><IT>R</IT><SUP>(&bgr;+1)</SUP>(<IT>R</IT><SUP>2</SUP> − <IT>R</IT><SUP>2</SUP><SUB>o</SUB>)</DE></FR> (2)
If beta  is 0, Eq. 2 equals Eq. A6. If both beta  and Ro are zero, Eq. 2 is appropriate for bubbles stabilized by a slowly permeating gas (23) and by the ideal surfactant discussed in APPENDIX B.


APPENDIX B

Mathematical Characterization of Stable Radii

In what follows, we develop equations that are applicable to bubbles stabilized by ideal gaseous surfactants and by slowly permeating gases (23) and are approximations for bubbles stabilized by other kinds of surfactant. This simplified case is convenient for mathematical manipulations; it uses a simplified form of Eq. 2 in which both Ro and beta  are zero
P<SUB>&Ggr;</SUB> = <FR><NU><IT>C</IT><SUB>&Ggr;</SUB></NU><DE><IT>R</IT><SUP>3</SUP></DE></FR> (B1)

By using Eq. 1 and Eq. B1, Eq. 3 can be written as a function of radius
&Dgr;Pabs = <FR><NU>2&ggr;</NU><DE><IT>R</IT></DE></FR> − <FR><NU><IT>C</IT><SUB><IT>&Ggr;</IT></SUB></NU><DE><IT>R</IT><SUP>3</SUP></DE></FR> + P<SUB>z</SUB> (B2)
When a bubble is at a stable radius R*, Delta Pabs = 0, so there is no net diffusion of gas between the bubble and its surroundings
P<SUB>z</SUB> = <FR><NU><IT>C</IT><SUB>&Ggr;</SUB></NU><DE><IT>R</IT>*<SUP>3</SUP></DE></FR> − <FR><NU>2&ggr;</NU><DE><IT>R</IT>*</DE></FR> (B3)
Unstressed radius. For one specific stable radius, there is no size-independent influence on the bubble; that is, Pz = 0. We refer to this as the "unstressed radius." Set Pz to zero in Eq. B3
<IT>R</IT><SUB>u</SUB>* = <FENCE><FR><NU><IT>C</IT><SUB>&Ggr;</SUB></NU><DE>2&ggr;</DE></FR></FENCE><SUP>0.5</SUP> (B4)
It is seen that R*u is a function of the ratio of the stabilization constant to the surface tension; examples of unstressed radii are seen at the intersections of the curves with the zero Pz axis in Figs. 2B and 3B.

Critical radius for irreversible growth. We next amplify on the contention, illustrated in Fig. 1C and 2A, that the maximum of a Sum curve on a Delta Pabs-vs.-radius plot is associated with an upper limit to the radius for a stabilized bubble. The limiting large size is brought about when addition of a strong growth pressure (negative Pz) brings the maximum of the Sum curve to the zero Delta Pabs axis. The smallest pressure at which the bubble is forced from a stable state into a state of unstable growth can be called the "critical growth pressure" (Pzg ), and the size of the bubble at that pressure can be called the "critical growth radius" (R*g).

The maximum of the Sum curve is found by equating the first derivative of Delta Pabs as a function of R (Eq. B2) to zero
<FR><NU>d(&Dgr;Pabs)</NU><DE>d<IT>R</IT></DE></FR> = <FR><NU>2&ggr;</NU><DE><IT>R</IT><SUP>2</SUP></DE></FR> − <FR><NU>3<IT>C</IT><SUB>&Ggr;</SUB></NU><DE><IT>R</IT><SUP>4</SUP></DE></FR> = 0 (B5)
The critical growth radius is the radius at which the bubble is both stable (Delta Pabs = 0) and at the maximum defined by Eq. B5
<IT>R</IT> <SUB>g</SUB>* = <FENCE><FR><NU>3<IT>C</IT><SUB>&Ggr;</SUB></NU><DE>2&ggr;</DE></FR></FENCE><SUP>0.5</SUP> (B6)
As with R*u in Eq. B4, R*g is a function of the ratio of the stabilization constant to the surface tension. Combination of Eqs. B4 and B6 shows that the growth radius is <RAD><RCD>3</RCD></RAD> times larger than the unstressed radius.

Putting Eq. B6 into Eq. B3 yields an expression for critical growth pressure as a function of C&Ggr;
P<SUB>z<SUB>g</SUB></SUB> = − <FR><NU>4</NU><DE>3</DE></FR> <FENCE><FR><NU>2&ggr;<SUP>3</SUP></NU><DE>3<IT>C</IT><SUB>&Ggr;</SUB></DE></FR></FENCE><SUP>0.5</SUP> (B7)
According to Eq. B7, bubbles with large C&Ggr; require less Pz to cause irreversible growth than bubbles with small C&Ggr;.

The dependence of critical growth radius on imposed Pz, seen as star  in Fig. 3B, is given by solving Eq. B6 for C&Ggr; and putting the result into Eq. B3
P<SUB>z<SUB>g</SUB></SUB> = − <FR><NU>4&ggr;</NU><DE>3<IT>R</IT> <SUB>g</SUB>*</DE></FR> (B8)
It is seen that Eq. B8 is analogous to the Laplace-Young equation: a pressure is inversely proportional to the first power of radius. Consonant with Eq. B8, the points for transition to irreversible growth (star ) in the cases shown in Figs. 3B, 4B, and 4D trace out paths in which Pz to cause growth is inversely related to radius.

Critical radius for crushing. We assume that a spherical, structurally stabilized bubble is crushed when its surface area is reduced to some particular small area at which the structural elements are pressed together maximally
4&pgr;<IT>R</IT> <SUB>c</SUB>*<SUP>2</SUP> = <IT>n A</IT><SUB>c</SUB> (B9)
where Ac is minimal area per structural element and n is number of structural elements. The maximal pressure that can be withstood is the "crushing pressure." An example of crushing behavior is the collapse of surface-active films at some maximal surface pressure (Ref. 1, p. 115) because the area approaches the minimal surface area of the aggregate of the molecules that comprise the film. Possibilities for action of the high surface pressure in a surfactant film include tearing of the stabilization mechanism, forcing part of the film to ride up over other parts, making the film transform into a "solid-phase" film that is no longer as compressible and cannot reexpand when absorptive forces are relieved (8), or "squeezing" some of the molecules of the surfactant out of the film (17).

The relation between C&Ggr; and the crushing radius is found by putting Eqs. A5 and B9 together and combining constants
<IT>C</IT><SUB>&Ggr;</SUB> = <FR><NU>2<IT>k</IT>T<IT>R</IT> <SUB>c</SUB>*<SUP>2</SUP></NU><DE><IT>A</IT><SUB>c</SUB></DE></FR> = <IT>bR</IT> <SUB>c</SUB>*<SUP>2</SUP> (B10)
The Ac in Eq. B10 defines the left-hand end of the P&Ggr; curves of Figs. 3A, 4A, and 4C; we made arbitrary choices for Ac to give the crushing radii for the Figs. 3A, 4A, and 4C.

We enter Eq. B10 into Eq. B3 to characterize the pattern of the filled diamonds in Fig. 3B
P<SUB>z<SUB>c</SUB></SUB> = <FR><NU><IT>b</IT> − 2&ggr;</NU><DE><IT>R</IT> <SUB>c</SUB>*</DE></FR> (B11)
According to Eq. B11, the Pz to cause crushing is a pressure equal to b/R*c minus the surface tension pressure at that radius (2gamma /R*c). The absorptive force of surface tension aids the external Pzc in the crushing phenomenon. As predicted by Eq. B11, the crushing points trace out paths inversely related to radius in Figs. 3B and 4D .

Recombination of variables shows that Pzc is inversely proportional to the square root of C&Ggr;
P<SUB>z<SUB>c</SUB></SUB> = (<IT>b</IT> − 2&ggr;) <FENCE><FR><NU><IT>b</IT></NU><DE><IT>C</IT><SUB>&Ggr;</SUB></DE></FR></FENCE><SUP>0.5</SUP> (B12)
The relations developed above were used to produce the diagrams in Figs. 1, 2, 3 and are in accord with the trends of the curves in Fig. 4, but do not apply to Fig. 5.


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