Academic literature on the topic 'Bubbly liquid'

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Journal articles on the topic "Bubbly liquid"

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Gao, Xin-Yi. "Density-fluctuation symbolic computation on the (3+1)-dimensional variable-coefficient Kudryashov–Sinelshchikov equation for a bubbly liquid with experimental support." Modern Physics Letters B 30, no. 15 (2016): 1650217. http://dx.doi.org/10.1142/s0217984916502171.

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Liquids with gas bubbles are commonly seen in medical science, natural science, daily life and engineering. Nonlinear-wave symbolic computation on the (3[Formula: see text]+[Formula: see text]1)-dimensional variable-coefficient Kudryashov–Sinelshchikov model for a bubbly liquid is hereby performed. An auto-Bäcklund transformation and some solitonic solutions are obtained. With respect to the density fluctuation of the bubble-liquid mixture, both the auto-Bäcklund transformation and solitonic solutions depend on the bubble-liquid-viscosity, transverse-perturbation, bubble-liquid-nonlinearity an
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Prakash, Vivek N., J. Martínez Mercado, Leen van Wijngaarden, et al. "Energy spectra in turbulent bubbly flows." Journal of Fluid Mechanics 791 (February 15, 2016): 174–90. http://dx.doi.org/10.1017/jfm.2016.49.

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We conduct experiments in a turbulent bubbly flow to study the nature of the transition between the classical $-5/3$ energy spectrum scaling for a single-phase turbulent flow and the $-3$ scaling for a swarm of bubbles rising in a quiescent liquid and of bubble-dominated turbulence. The bubblance parameter (Lance & Bataille J. Fluid Mech., vol. 222, 1991, pp. 95–118; Rensen et al., J. Fluid Mech., vol. 538, 2005, pp. 153–187), which measures the ratio of the bubble-induced kinetic energy to the kinetic energy induced by the turbulent liquid fluctuations before bubble injection, is often us
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Jia, Zheng, Mingjun Pang, and Ruipeng Niu. "Numerical Investigation on Effect of Bubbles Arrangement and Volume Fraction on Apparent Viscosity of Bubbly Suspensions." Recent Innovations in Chemical Engineering (Formerly Recent Patents on Chemical Engineering) 16, no. 4 (2023): 285–304. http://dx.doi.org/10.2174/0124055204268474230922054143.

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Background:: Bubbly suspensions can be often run into in natural and industrial processes. The addition of bubbles with different sizes can lead to a significant change in the rheological properties of a matrix liquid. It is extremely significant to fully understand the rheological properties of bubbly suspensions for improving process efficiencies and optimizing productive processes. background: Bubbly suspensions can be often run into in natural and industrial processes. The addition of bubbles of different sizes can greatly change the rheological properties of matrix liquid. It is extremely
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Serbout, Sanae, Laurent Maxit, and Frédéric Michel. "Vibration of a stiffened pipe filled with a bubbly liquid: analysis of resonance frequencies in function of bubble fraction." INTER-NOISE and NOISE-CON Congress and Conference Proceedings 263, no. 5 (2021): 1008–18. http://dx.doi.org/10.3397/in-2021-1730.

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The characterization of the presence of bubbles in industrial fluid circuits may be extremely important for many safety issuses. It is well known that the acoustic properties of liquids can be drastically modified by a small amount of gaz content in the liquid. At sufficiently low frequencies, the speed of sound depends primarily on the gas volume fraction. The variation of the gas fraction may then induce some variations in the vibroacoustic behavior of the pipe transporting the liquid. Analysis of the pipe vibrations can then help in the monitoring of the bubble presence. In such a context,
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MUDDE, ROBERT F., and TAKAYUKI SAITO. "Hydrodynamical similarities between bubble column and bubbly pipe flow." Journal of Fluid Mechanics 437 (June 22, 2001): 203–28. http://dx.doi.org/10.1017/s0022112001004335.

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The hydrodynamical similarities between the bubbly flow in a bubble column and in a pipe with vertical upward liquid flow are investigated. The system concerns air/water bubbly flow in a vertical cylinder of 14.9 cm inner diameter. Measurements of the radial distribution of the liquid velocity, gas fraction and the bubble velocity and size are performed using laser Doppler anemometry for the liquid velocity and a four-point optical fibre probe for the gas fraction, bubble velocity and size. The averaged gas fraction was 5.2% for the bubble column (with a superficial liquid velocity of zero) an
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Wang, Yu, Dehua Chen, Xueshen Cao, and Xiao He. "Theoretical and Experimental Studies of Acoustic Reflection of Bubbly Liquid in Multilayer Media." Applied Sciences 12, no. 23 (2022): 12264. http://dx.doi.org/10.3390/app122312264.

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Bubbly liquids are widely present in the natural environment and industrial fields, such as seawater near the ocean bottom, the multiphase flow in petroleum reservoirs, and the blood with bubbles resulting in decompression sickness. Therefore, accurate measurement of the gas content is of great significance for hydroacoustic physics, oil and gas resources exploration, and disease prevention and diagnosis. Trace bubbles in liquids can lead to considerable changes in the acoustic properties of gas–liquid two-phase media. Acoustic measurements can therefore be applied for trace bubble detection.
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Reeder, D. Benjamin, John E. Joseph, Thomas A. Rago, Jeremy M. Bullard, David Honegger, and Merrick C. Haller. "Acoustic spectrometry of bubbles in an estuarine front: Sound speed dispersion, void fraction, and bubble density." Journal of the Acoustical Society of America 151, no. 4 (2022): 2429–43. http://dx.doi.org/10.1121/10.0009923.

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Estuaries constitute a unique waveguide for acoustic propagation. The spatiotemporally varying three-dimensional front between the seawater and the outflowing freshwater during both flood and ebb constitutes an interfacial sound speed gradient capable of supporting significant vertical and horizontal acoustic refraction. The collision of these two water masses often produces breaking waves, injecting air bubbles into the water column; the negative vertical velocities of the denser saltwater often subduct bubbles to the bottom of these shallow waveguides, filling the water column with a bubbly
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Fattakhov, S. R. "Study of pressure wave dynamics in a channel with a spherical bubble cluster." Multiphase Systems 18, no. 1 (2023): 27–31. http://dx.doi.org/10.21662/mfs2023.1.004.

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The features of wave propagation in a bubbly liquid are associated with the combined interaction of nonlinear, dispersive, and dissipative effects. In a liquid with bubbles, the properties of a practically incompressible liquid, which is a carrier phase, change dramatically with a small volume (and even more so, mass) addition of gas (bubbles), which is a dispersed phase. The peculiarity of bubbly liquids is due to their high static compressibility while maintaining a high density close to that of the liquid, which in turn leads to a low equilibrium speed of sound. In this paper, we study two-
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Lu, Tianshi, Roman Samulyak, and James Glimm. "Direct Numerical Simulation of Bubbly Flows and Application to Cavitation Mitigation." Journal of Fluids Engineering 129, no. 5 (2006): 595–604. http://dx.doi.org/10.1115/1.2720477.

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The direct numerical simulation (DNS) method has been used to the study of the linear and shock wave propagation in bubbly fluids and the estimation of the efficiency of the cavitation mitigation in the container of the Spallation Neutron Source liquid mercury target. The DNS method for bubbly flows is based on the front tracking technique developed for free surface flows. Our front tracking hydrodynamic simulation code FronTier is capable of tracking and resolving topological changes of a large number of interfaces in two- and three-dimensional spaces. Both the bubbles and the fluid are compr
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Ekambara, K., R. Sean Sanders, K. Nandakumar, and J. H. Masliyah. "CFD Modeling of Gas-Liquid Bubbly Flow in Horizontal Pipes: Influence of Bubble Coalescence and Breakup." International Journal of Chemical Engineering 2012 (2012): 1–20. http://dx.doi.org/10.1155/2012/620463.

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Modelling of gas-liquid bubbly flows is achieved by coupling a population balance equation with the three-dimensional, two-fluid, hydrodynamic model. For gas-liquid bubbly flows, an average bubble number density transport equation has been incorporated in the CFD code CFX 5.7 to describe the temporal and spatial evolution of the gas bubbles population. The coalescence and breakage effects of the gas bubbles are modeled. The coalescence by the random collision driven by turbulence and wake entrainment is considered, while for bubble breakage, the impact of turbulent eddies is considered. Local
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Dissertations / Theses on the topic "Bubbly liquid"

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Lai, Huanxin. "Simulation of two-phase bubbly flows : an inert bubble introduced into a hot liquid." Thesis, Nottingham Trent University, 2003. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.271735.

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楊兆麟 and Siu-lun Patrick Yeung. "Effect of bubbly liquid on underwater sound transmission." Thesis, The University of Hong Kong (Pokfulam, Hong Kong), 1998. http://hub.hku.hk/bib/B31237964.

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Yeung, Siu-lun Patrick. "Effect of bubbly liquid on underwater sound transmission /." Hong Kong : University of Hong Kong, 1998. http://sunzi.lib.hku.hk/hkuto/record.jsp?B19471221.

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Leonard, S. R. "The propagation of nonlinear waves in a bubbly liquid." Thesis, University of Leeds, 1988. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.235334.

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Shi, Jun-Mei, Horst-Michael Prasser, and Ulrich Rohde. "Turbulent dispersion of bubbles in poly-dispersed gas-liquid flows in a vertical pipe." Forschungszentrum Dresden, 2010. http://nbn-resolving.de/urn:nbn:de:bsz:d120-qucosa-28046.

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Turbulence dispersion is a phenomenon of practical importance in many multiphase flow systems. It has a strong effect on the distribution of the dispersed phase. Physically, this phenomenon is a result of interactions between individual particles of the dispersed phase and the continuous phase turbulence eddies. In a Lagrangian simulation, a particle-eddy interaction sub-model can be introduced and the effect of turbulence dispersion is automatically accounted for during particle tracking. Nevertheless, tracking of particleturbulence interaction is extremely expensive for the small time steps
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Shi, Jun-Mei, Horst-Michael Prasser, and Ulrich Rohde. "Turbulent dispersion of bubbles in poly-dispersed gas-liquid flows in a vertical pipe." Forschungszentrum Dresden-Rossendorf, 2007. https://hzdr.qucosa.de/id/qucosa%3A21631.

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Turbulence dispersion is a phenomenon of practical importance in many multiphase flow systems. It has a strong effect on the distribution of the dispersed phase. Physically, this phenomenon is a result of interactions between individual particles of the dispersed phase and the continuous phase turbulence eddies. In a Lagrangian simulation, a particle-eddy interaction sub-model can be introduced and the effect of turbulence dispersion is automatically accounted for during particle tracking. Nevertheless, tracking of particleturbulence interaction is extremely expensive for the small time steps
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Zhang, Hongna. "Study on Upward Turbulent Bubbly Flow in Ducts." 京都大学 (Kyoto University), 2014. http://hdl.handle.net/2433/192190.

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Suñol, Galofré Francesc. "Bubble and droplet flow phenomena at different gravity levels." Doctoral thesis, Universitat Politècnica de Catalunya, 2011. http://hdl.handle.net/10803/32305.

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Two-phase flows are encountered in a wide range of applications both on-ground and in space. The dynamics of such flows in the absence of gravity is completely different from that in normal gravity due to the absence of buoyancy forces. A deeper understanding of the behavior of multiphase flows is essential in order to improve the operation of devices which require the use of two-phase systems. Analytical and experimental work is still needed for enhancing the control of two-phase flows, due to the theoretical complexity and the lack of experimental data for certain configurations. In this wo
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Ilić, Milica. "Statistical analysis of liquid phase turbulence based on direct numerical simulations of bubbly flows." Karlsruhe : FZKA, 2006. http://nbn-resolving.de/urn:nbn:de:0005-071995.

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Shawkat, Mohamed Ezz El-Din Ibrahim Saleh Ching Chan Y. Shoukri Mamdouh. "Liquid turbulence structure in two-phase bubbly flow in a large diameter vertical pipe." *McMaster only, 2007.

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Books on the topic "Bubbly liquid"

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Laari, Arto. Gas-liquid mass transfer in bubbly flow: Estimation of mass transfer, bubble size and reactor performance in various applications. Lappeenranta University of Technology, 2005.

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Katsumi, Tsuchiya, ed. Bubble wake dynamics in liquids and liquid-solid suspensions. Butterworth-Heinemann, 1990.

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T, Long Y., and United States. National Aeronautics and Space Administration., eds. Bubble mass center and fluid feedback force fluctuations activated by constant lateral impulse with variable thrust. National Aeronautics and Space Administration, 1995.

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Reinke, Peter. Surface boiling of superheated liquid. Paul Scherrer Institute, Labor für Thermohydraulik, 1997.

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Fujikawa, Shigeo, Takeru Yano, and Masao Watanabe. Vapor-Liquid Interfaces, Bubbles and Droplets. Springer Berlin Heidelberg, 2011. http://dx.doi.org/10.1007/978-3-642-18038-5.

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Dasgupta, Subhachari. Determination of the dispersion constant in a constrained vapor bubble thermosyphon. National Aeronautics and Space Administration, 1993.

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D'Arrigo, Joseph S. Stable gas-in-liquid emulsions: Production in natural waters and artificial media. Elsevier, 1985.

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Kalis, Aouni A. Liquid phase velocity of turbulent dispersed bubbles flow in large diameter horizontal pipes. Ecole polytechnique de Montreal, Departement de genie mecanique, Section mecanique appliquee, 1988.

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United States. National Aeronautics and Space Administration., ed. Numerical studies of surface tensions: Final research report. University of Alabama in Huntsville, 1995.

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L, Pan H., and United States. National Aeronautics and Space Administration., eds. Mathematical model of bubble sloshing dynamics for cryogenic liquid helium in orbital spacecraft dewar container. Elsevier Science, Inc., 1995.

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Book chapters on the topic "Bubbly liquid"

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Kuzmin, Dmitri, and Stefan Turek. "Finite Element Discretization Tools for Gas-Liquid Flows." In Bubbly Flows. Springer Berlin Heidelberg, 2004. http://dx.doi.org/10.1007/978-3-642-18540-3_15.

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van Sint Annaland, M., N. G. Deen, and J. A. M. Kuipers. "Multi-Level Modelling of Dispersed Gas-Liquid Two-Phase Flows." In Bubbly Flows. Springer Berlin Heidelberg, 2004. http://dx.doi.org/10.1007/978-3-642-18540-3_12.

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Scheid, S., S. John, O. Bork, H. Parchmann, M. Schlüter, and N. Räbiger. "Improved model for the calculation of homogeneous gas-liquid flows." In Bubbly Flows. Springer Berlin Heidelberg, 2004. http://dx.doi.org/10.1007/978-3-642-18540-3_7.

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Kertzscher, U., A. Seeger, K. Affeld, and E. Wellnhofer. "Simultaneous measurement of the local liquid and the local solid velocities." In Bubbly Flows. Springer Berlin Heidelberg, 2004. http://dx.doi.org/10.1007/978-3-642-18540-3_22.

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Bourloutski, E., and M. Sommerfeld. "Euler/Lagrange Calculations of Gas-Liquid-Solid-Flows in Bubble Columns with Phase Interaction." In Bubbly Flows. Springer Berlin Heidelberg, 2004. http://dx.doi.org/10.1007/978-3-642-18540-3_19.

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Borchers, Oliver, and Gerhart Eigenberger. "Detailed experimental studies on gas-liquid bubble flow in bubble columns with and without recycle." In Bubbly Flows. Springer Berlin Heidelberg, 2004. http://dx.doi.org/10.1007/978-3-642-18540-3_2.

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Gast, Sebastian, Ute Tuttlies, and Ulrich Nieken. "Determination of Intrinsic Gas-Liquid Reaction Kinetics in Homogeneous Liquid Phase and the Impact of the Bubble Wake on Effective Reaction Rates." In Reactive Bubbly Flows. Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-72361-3_10.

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Prosperetti, Andrea. "Linear Waves in Bubbly Liquids." In IUTAM Symposium on Waves in Liquid/Gas and Liquid/Vapour Two-Phase Systems. Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0057-1_4.

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Beylich, Alfred E. "Pressure Waves in Bubbly Liquids." In IUTAM Symposium on Waves in Liquid/Gas and Liquid/Vapour Two-Phase Systems. Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0057-1_7.

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Beylich, Alfred E., and Ali Gülhan. "Waves in Reactive Bubbly Liquids." In Adiabatic Waves in Liquid-Vapor Systems. Springer Berlin Heidelberg, 1990. http://dx.doi.org/10.1007/978-3-642-83587-2_4.

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Conference papers on the topic "Bubbly liquid"

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Mahmood, Shahid, Yungpil Yoo, and Ho-Young Kwak. "Pressure and Shock Waves in Bubbly Liquids." In ASME/JSME/KSME 2015 Joint Fluids Engineering Conference. American Society of Mechanical Engineers, 2015. http://dx.doi.org/10.1115/ajkfluids2015-05047.

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It is well known that sound propagation in liquid media is strongly affected by the presence of gas bubbles that interact with sound and in turn affect the medium. An explicit form of a wave equation in a bubbly liquid medium was obtained in this study. Using the linearized wave equation and the Keller-Miksis equation for bubble wall motion, a dispersion relation for the linear pressure wave propagation in bubbly liquids was obtained. It was found that attenuation of the waves in bubbly liquid occurs due to the viscosity and the heat transfer from/to the bubble. In particular, at the lower fre
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Sun, HaoMin, Tomoaki Kunugi, DaZhuan Wu, HongNa Zhang, Hideo Nakamura, and XiuZhong Shen. "Gas-Liquid Bubbly Turbulent Upward Flow in Square Duct." In 2012 20th International Conference on Nuclear Engineering and the ASME 2012 Power Conference. American Society of Mechanical Engineers, 2012. http://dx.doi.org/10.1115/icone20-power2012-54918.

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As for the turbulent two-phase flow in the non-circular duct, the flow could show an anisotropic turbulence feature in liquid phase. In this study, the air-water bubbly turbulent upward flow experiment in the large square duct with the inside cross-section of 136mm×136mm has been conducted. Since the bubble size is very important for air-water bubbly flows, the bubble generating method was improved to get more uniform bubble size. After confirming the flow symmetry in the measuring cross-section, the distributions of local void fraction, bubble frequency and primary liquid velocity were measur
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Murakawa, Hideki, Hiroshige Kikura, Masanori Aritomi, and Michitsugu Mori. "Measurement of Bubbly Flow in a Vertical Pipe Using Ultrasonic Doppler Method." In ASME/JSME 2003 4th Joint Fluids Summer Engineering Conference. ASMEDC, 2003. http://dx.doi.org/10.1115/fedsm2003-45384.

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In order to clarify the microscopic flow structure, the ultrasonic Doppler method was applied to the measurement of two-phase bubbly flow in vertical pipe (i.d.50mm). Liquid flow structure might strongly be influenced by the characteristic of the injected bubbles, i.e. bubbles’ size and void fraction. In this study, a bubble generator was newly designed with the purpose to control the bubble size and void fraction, independent of liquid main-flow rate. The experiment was performed at z/d = 66 from the bubble generator. Liquid flow rates were of the Reynolds numbers ranging from Rem = 3700 to 6
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Yoshida, Kohei, Kota Fujiwara, Akiko Kaneko, and Yutaka Abe. "Experimental Study on Bubble and Aerosol Behavior During Pool Scrubbing." In 2021 28th International Conference on Nuclear Engineering. American Society of Mechanical Engineers, 2021. http://dx.doi.org/10.1115/icone28-61490.

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Abstract Understanding radioactive aerosol behavior is important during severe accidents in nuclear power plants. In particular, pool scrubbing at a suppression pool is a key factor for estimating the leakage of radioactive aerosol into the environment. Therefore, we have to elucidate the mechanism of the aerosol transfer from the gas phase to the liquid phase during bubbly flow. Currently, models to evaluate the amount of aerosol removal by pool scrubbing have been incorporated into integrated severe accident analysis codes such as MELCOR. However, the models for bubbles and aerosols behavior
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Hiroi, Takamichi, Tatsuya Hamada, and Chiharu Kawakita. "Investigation on the Characteristic of Bubbles in Horizontal Channel Flow by Fiber Optic Sensor." In ASME-JSME-KSME 2019 8th Joint Fluids Engineering Conference. American Society of Mechanical Engineers, 2019. http://dx.doi.org/10.1115/ajkfluids2019-4646.

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Abstract Friction drag and characteristic of bubbles in horizontal water channel are investigated at bulk liquid velocity Um = 1 ∼ 5 m/s (Reynolds number Rem = 16,000 ∼ 120,000 (based on the channel height)) and mean void fraction α = 0.5, 1, 2 %. Firstly, shear stress sensor is applied to investigate the relation between friction drag with bubbles and bulk liquid velocity. Friction drag in the bubbly flow is larger than it in the single-phase flow at Um = 1 ∼ 2 m/s. It in the bubbly flow, however, decreases with the mean liquid velocity. Furthermore, it in bubbly flow is smaller than it in th
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Garbaly, Aleksey, and Thomas Shepard. "Impact of Bubble Size on Flow Response to Transient Pressure Drop Through Converging Nozzle." In ASME 2020 Fluids Engineering Division Summer Meeting collocated with the ASME 2020 Heat Transfer Summer Conference and the ASME 2020 18th International Conference on Nanochannels, Microchannels, and Minichannels. American Society of Mechanical Engineers, 2020. http://dx.doi.org/10.1115/fedsm2020-20278.

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Abstract For homogenous two-phase bubbly flows, the theoretical speed of sound is dramatically reduced at moderate void fractions to speeds much lower than the speed of sound for either single phase. This theoretical speed of sound would suggest a propensity for bubbly flows to reach choked conditions when traveling through a convergent nozzle. However, for a bubbly flow to be considered homogenous requires assumptions that may not be realized in practical applications. In this experimental study, a bubbly flow was sent through a convergent nozzle before entering a large chamber. By setting st
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Kataoka, Isao, Kenji Yoshida, Tsutomu Ikeno, Tatsuya Sasakawa, and Koichi Kondo. "Analysis of Turbulence Structure and Void Fraction Distribution in Gas-Liquid Two-Phase Flow Under Bubbly and Slug Flow Regime." In ASME-JSME-KSME 2011 Joint Fluids Engineering Conference. ASMEDC, 2011. http://dx.doi.org/10.1115/ajk2011-10003.

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Accurate analyses of turbulence structure and void fraction distribution are quite important in designing and safety evaluation of various industrial equipments using gas-liquid two-phase flow such as nuclear reactor, etc. Using turbulence model of two-phase flow and models of bubble behaviors in bubble flow and slug flow, systematic analyses of distributions of void fraction, averaged velocity and turbulent velocity were carried out and compared with experimental data. In bubbly flow, diffusion of bubble and lift force are dominant in determining void fraction distribution. On the other hand,
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Roy, Ramendra P. "On the Structure of Turbulent Bubbly Gas-Liquid Flows." In ASME 1997 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 1997. http://dx.doi.org/10.1115/imece1997-0762.

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Abstract To gain understanding of the structure of turbulent bubbly gas (or vapor)-liquid flows, local measurements have been carried out in the bubbly regime of isothermal gas-liquid flow and boiling flow. The isothermal flow was created by injecting nitrogen gas into an upward flow of liquid Refrigerant-113 through a vertical pipe. The boiling flow, of Refrigerant-113, was created in a vertical annular channel whose inner wall was heated. In both flows, the radial distributions of gas (or vapor) residence time fraction, bubble mean axial velocity, and bubble diameter were measured by a dual-
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Matsumoto, Yoichiro, Hideji Nishikawa, Taku Ohara, and Hideo Ohashi. "Pressure wave phenomena in bubbly liquid." In Current topics in shock waves 17th international symposium on shock waves and shock tubes Bethlehem, Pennsylvania (USA). AIP, 1990. http://dx.doi.org/10.1063/1.39477.

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Esmaeeli, Asghar, Chan Ching, and Mamdouh Shoukri. "Phase Distribution in Buoyancy-Driven Bubbly Flows." In ASME 2002 Joint U.S.-European Fluids Engineering Division Conference. ASMEDC, 2002. http://dx.doi.org/10.1115/fedsm2002-31236.

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This study aims to investigate the effect of topology change on the rise velocity of bubbly flows and the phase distribution in a channel at a moderate Reynolds number. A front tracking/finite difference method is used to solve the momentum equation inside and outside deformable bubbles. It is found that bubble/bubble coalescence enhances the average rise velocity of the bubbles dramatically and also increases the fluctuations of the liquid velocity. Examination of the pair distribution function shows that the flow becomes more non-homogeneous as a result of topology change.
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Reports on the topic "Bubbly liquid"

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Carney, Janine, Felipe Maciel, and Paulo Waltrich. Evaluation of a CFD Commercial Package to the Modeling of Acoustic Wave Propagation in Bubbly-Liquid Column. Office of Scientific and Technical Information (OSTI), 2023. http://dx.doi.org/10.2172/2221796.

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Kushner, Mark. Plasmas in Multiphase Media: Bubble Enhanced Discharges in Liquids and Plasma/Liquid Phase Boundaries. Office of Scientific and Technical Information (OSTI), 2014. http://dx.doi.org/10.2172/1136529.

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Chang X., E. Wang, and T. Xin. Effects of Liquid Helium Bubble Formation in a Superconducting Cavity Cryogenic System. Office of Scientific and Technical Information (OSTI), 2011. http://dx.doi.org/10.2172/1061976.

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Hamaguchi, H., and T. Sakaguchi. Velocity of large bubble in liquid-solid mixture in a vertical tube. Office of Scientific and Technical Information (OSTI), 1995. http://dx.doi.org/10.2172/106992.

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Chang, X., E. Wang, and T. Xin. Effects of liquid helium bubble formation in a superconducting cavity cryogenic system. Office of Scientific and Technical Information (OSTI), 2011. http://dx.doi.org/10.2172/1030635.

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McMullen, Ryan, and John Torczynski. Evaluation of the Barracuda Software Package for Simulating Bubble Motion in Vibrating Liquid-Filled Containers. Office of Scientific and Technical Information (OSTI), 2021. http://dx.doi.org/10.2172/1821976.

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Nadim, Ali, Paul E. Barbone, and Jerome J. Cartmell. Shock Propagation and Attenuation in Bubbly Liquids: Modeling Wave Propagation Using a Nonlinear Equation-of-State. Defense Technical Information Center, 1999. http://dx.doi.org/10.21236/ada370801.

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Lambert, Hugues. Study of a double bubbler for material balance in liquids. Office of Scientific and Technical Information (OSTI), 2013. http://dx.doi.org/10.2172/1097166.

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Duignan, M. R., and A. B. Barnes. Development of Liquid Level and Density Bubbler for DWPF Canyon Vessels. Final report. Office of Scientific and Technical Information (OSTI), 1994. http://dx.doi.org/10.2172/10116510.

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Collar, J. I., M. Crisler, J. Hall, et al. COUPP, a Heavy-Liquid Bubble Chamber for WIMP Detection: First Tests in the MINOS Near-Detector Gallery. Office of Scientific and Technical Information (OSTI), 2004. http://dx.doi.org/10.2172/993555.

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