2015
DOI: 10.1017/jfm.2015.436
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Mass transfer effects on linear wave propagation in diluted bubbly liquids

Abstract: In this article we investigate the importance of mass transfer effects in the effective acoustic properties of diluted bubbly liquids. The classical theory for wave propagation in bubbly liquids for pure gas bubbles is extended to capture the influence of mass transfer on the effective phase speed and attenuation of the system. The vaporization flux is shown to be important for systems close to saturation conditions and at low frequencies. We derive a general expression for the transfer function that relates b… Show more

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Cited by 63 publications
(68 citation statements)
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“…Quantity ρ b is the density of the air‐vapor mixture in the bubble, and DnormalbnormalM is the mass diffusion coefficient of vapor in air. For the heat flux, Fuster and Montel () defined the difference of the conductive heat flux in the liquid and the bubble to be equal to the vaporization enthalpy Δ H vap times the total mass flux across the interface, κnormallTnormall∂rκnormalbTnormalb∂r=Hvap2.56804pt2.56804ptat2.56804pt2.56804ptr=R, where κ l and κ b are the thermal conductivities, T l and T b are the temperatures, and the subscripts b and l refer to the liquid and bubble phase, respectively. In equations and , the total mass flux of water across the bubble‐liquid interface, J ( r = R ) is equal to the amount of vapor that undergoes phase change.…”
Section: Effective Fluid Propertiesmentioning
confidence: 99%
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“…Quantity ρ b is the density of the air‐vapor mixture in the bubble, and DnormalbnormalM is the mass diffusion coefficient of vapor in air. For the heat flux, Fuster and Montel () defined the difference of the conductive heat flux in the liquid and the bubble to be equal to the vaporization enthalpy Δ H vap times the total mass flux across the interface, κnormallTnormall∂rκnormalbTnormalb∂r=Hvap2.56804pt2.56804ptat2.56804pt2.56804ptr=R, where κ l and κ b are the thermal conductivities, T l and T b are the temperatures, and the subscripts b and l refer to the liquid and bubble phase, respectively. In equations and , the total mass flux of water across the bubble‐liquid interface, J ( r = R ) is equal to the amount of vapor that undergoes phase change.…”
Section: Effective Fluid Propertiesmentioning
confidence: 99%
“…In equations and , the total mass flux of water across the bubble‐liquid interface, J ( r = R ) is equal to the amount of vapor that undergoes phase change. Fuster and Montel () defined this mass flux, which is driven by the evaporation and condensation at the surface of the bubble, by the Hertz‐Knudsen‐Langmuir (see Fuster & Montel, , and references therein) expression to be J(r=R)=αevapPeqnormalIPb,vapornormalI2πRspecTint. …”
Section: Effective Fluid Propertiesmentioning
confidence: 99%
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“…The problem of small disturbance propagation in a liquid with gas-vapor bubbles in some or another formulation was studied in [20][21][22][23][24][25][26][27][28][29][30][31][32][33].…”
Section: Introductionmentioning
confidence: 99%