1975
DOI: 10.1016/0301-9322(75)90013-0
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Turbulence structure of air-water bubbly flow—III. transport properties

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Cited by 103 publications
(42 citation statements)
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“…These instantaneous fluctuations cause bubble deformations which themselves react to the perturbation by producing chaotic and highly variable flow fields organized as eddies (Serizawa et al, 1975;Schlüter, 2002). With increasing gas contents, the bubble-induced turbulences become more dominant resulting in an increased flow resistance.…”
Section: Frequency Distributionsmentioning
confidence: 99%
“…These instantaneous fluctuations cause bubble deformations which themselves react to the perturbation by producing chaotic and highly variable flow fields organized as eddies (Serizawa et al, 1975;Schlüter, 2002). With increasing gas contents, the bubble-induced turbulences become more dominant resulting in an increased flow resistance.…”
Section: Frequency Distributionsmentioning
confidence: 99%
“…(95)), the radial distributions of interfacial area concentration are predicted and compared with experimental data. Serizawa et al (1975Serizawa et al ( , 1992 For empirical coefficient, K cai is assumed to be 0.01 based o n e x p e r i m e n t a l d a t a . T h e condition of flow regime transition from bubbly to churn flow is given in terms of area averaged void fraction,  based on experimental results which is given by…”
Section: Experimental Researches On Interfacial Area Concentrationmentioning
confidence: 99%
“…Only one study has reported vapor turbulence measurements in &-water annular flows with a liquid film interface (Azzopardi and Teixeira, 1994b). They concluded that turbulence intensities were higher than the values that would Hot-film anemometry (HFA) techniques have been used extensively for local turbulence measurements in both bubbly flow (Serizawa et al, 1975;h@chiyoshi and Serizawa, 1986;Wang et al, 1990;Lance and Bataille, 1991;Hogsett and Ishii, 1997) and dropletlparticle flows (Ginzburg, 1971;Hetsroni and Sokolov, 1971 The specific objectives of the present study are to: a) extend the established hot-film anemometer technique for turbulence measurements in refrigerant flows using a dual-sensor probe, b) perform drop size and turbulence measurements in the vapor core at gas-liquid density ratios comparable to steam-water at high pressure, and c) provide insight into the complex physical phenomena characteristic of turbulent, annular two-phase flows.…”
Section: Introductionmentioning
confidence: 99%