1991
DOI: 10.1016/0301-9322(91)90029-3
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Analysis of phase distribution in fully developed laminar bubbly two-phase flow

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Cited by 758 publications
(329 citation statements)
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“…The studies done in bubbly vertical downward flow by Drew and Lahey [6], Wang et al [7] Antal et al [8] and Kashinsky and Randin [5] reported similar void fraction distributions as measured in the current study with a quasi-constant void fraction in the core region which drops abruptly to zero as the wall is approached. Iskandrani and Kojasoy [9] also reported that, in twophase vertical bubbly flows, the presence of voids tends to flatten the liquid velocity profile, thus leading to a homogenous phase distribution across the vertical pipe section.…”
Section: Resultssupporting
confidence: 85%
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“…The studies done in bubbly vertical downward flow by Drew and Lahey [6], Wang et al [7] Antal et al [8] and Kashinsky and Randin [5] reported similar void fraction distributions as measured in the current study with a quasi-constant void fraction in the core region which drops abruptly to zero as the wall is approached. Iskandrani and Kojasoy [9] also reported that, in twophase vertical bubbly flows, the presence of voids tends to flatten the liquid velocity profile, thus leading to a homogenous phase distribution across the vertical pipe section.…”
Section: Resultssupporting
confidence: 85%
“…Furthermore, Antal et al [8] related the void fraction distribution across the vertical pipe section with a wall repulsion force dependent on the bubble radius, distance from the wall and the phase relative velocity. Such a repulsion force is assumed to be equal for both down and upward flows.…”
Section: Resultsmentioning
confidence: 99%
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“…It is mainly determined by the lift and wall forces. Antal et al [14] proposed a wall lubrication force as follows: …”
Section: Wall Lubrication Force Modelmentioning
confidence: 99%
“…The lift force is given by where CD is the lift force coefficient given by the Tomiyama correlation [23]. The wall lubrication [24] and turbulent dispersion [25] forces are also implemented to consider the lateral motion of gas in liquid. The virtual mass force is expressed as where For the interfacial heat transfer coefficients in Eqs.…”
Section: Physical Modelsmentioning
confidence: 99%