1991
DOI: 10.1017/s0022112091001015
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Turbulence in the liquid phase of a uniform bubbly air–water flow

Abstract: The paper describes studies of the turbulence of the liquid in a bubbly, grid-generated turbulent flow field. Laser-Doppler and hot-film anemometry are used for the experimental investigation. It is found that the turbulent kinetic energy increases strongly with the void fraction α. Roughly speaking, there exist two distinct regimes: the first one corresponds to low value of α, where hydrodynamic interactions between bubbles are negligible, and the second one to higher values, for which, owing to their mutual … Show more

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Cited by 490 publications
(368 citation statements)
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“…Point (ii) constitutes a major difference since classic turbulence is unlikely to be able to maintain vertical homogeneity when upside-down symmetry is broken, non-zero dissymmetry coefficients being usually associated with a turbulence gradient (Risso & Fabre 1997). A second difference is that the spectral signature of bubble-induced turbulence differs from the classic K5/3 power law (Lance & Bataille 1991), indicating that the dynamics of the fluctuating eddies is different. The bubbleinduced turbulence is commonly considered as a turbulence in which energy is injected at an intermediate scale close to the bubble diameter instead of being supplied by the largest scales of the flow.…”
Section: Perspectivesmentioning
confidence: 99%
“…Point (ii) constitutes a major difference since classic turbulence is unlikely to be able to maintain vertical homogeneity when upside-down symmetry is broken, non-zero dissymmetry coefficients being usually associated with a turbulence gradient (Risso & Fabre 1997). A second difference is that the spectral signature of bubble-induced turbulence differs from the classic K5/3 power law (Lance & Bataille 1991), indicating that the dynamics of the fluctuating eddies is different. The bubbleinduced turbulence is commonly considered as a turbulence in which energy is injected at an intermediate scale close to the bubble diameter instead of being supplied by the largest scales of the flow.…”
Section: Perspectivesmentioning
confidence: 99%
“…In this context, the description of the liquid agitation is a key issue. In the most general situation, such as that encountered in an industrial bubble column, the agitation has different sources: (1) the bubble-induced agitation that results from the flow disturbances generated by bubble motions (Lance & Bataille 1991;Cartellier & Rivière 2001;Zenit, Koch & Sangani 2001;Risso & Ellingsen 2002), (2) the buoyancy-driven recirculation cells that develop as soon as the volume fraction is not uniform (Climent & Magnaudet 1999;Mudde 2005), and (3) the turbulence produced by mean shear (Larue de Tournemine & Roig 2010;Prakash et al 2016). The present work focuses on the bubble-induced agitation at large Reynolds number, i.e.…”
Section: Introductionmentioning
confidence: 99%
“…Details of the database are provided in Table 1 smaller bubbles are included for downward flow conditions only (0.8 mm and 1.5 mm). In 299 addition, comparison is also provided against grid-generated turbulence data obtained for 300 bubbly flows by Lance and Bataille (1991). Since these data were only used for validating 301 predictions of the axial development of the turbulence, they are not included in Table 1 it is important to stress the necessity of detailed experimental studies for proper model 315 validation.…”
mentioning
confidence: 99%