2004
DOI: 10.1016/j.ces.2003.11.018
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Modelling of dispersed bubble and droplet flow at high phase fractions

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Cited by 202 publications
(132 citation statements)
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“…The main difficulty for this class of problems is not only the usual one for fluids pertaining to the free-surface flow (e.g. see [22,42,33,5,72,70,71]) but also the fluid-structure interface. Providing reliable description at the interface for a fluid-structure interaction problem is quite a challenge, since the descriptions generally used for each of the sub-problems are different: for the structure part, it is natural to follow material point motion in a Lagrangian formulation, while an Eulerian formulation is often preferred 1 for the fluid part.…”
Section: Introductionmentioning
confidence: 99%
“…The main difficulty for this class of problems is not only the usual one for fluids pertaining to the free-surface flow (e.g. see [22,42,33,5,72,70,71]) but also the fluid-structure interface. Providing reliable description at the interface for a fluid-structure interaction problem is quite a challenge, since the descriptions generally used for each of the sub-problems are different: for the structure part, it is natural to follow material point motion in a Lagrangian formulation, while an Eulerian formulation is often preferred 1 for the fluid part.…”
Section: Introductionmentioning
confidence: 99%
“…Even if further verification is 501 required for flows with significant void fraction (Behzadi et al, 2004), at the present time this 502 approach is applied to the whole database, as done in the majority of the previous works 503 …”
mentioning
confidence: 99%
“…Indeed, experimental measurements 510 suggest that a value of unity is approached starting from void fractions as small as 6 % 511 (Behzadi et al, 2004). 512…”
mentioning
confidence: 99%
“…Among these interphase forces, the drag force, → F drag , is the dominant component. The drag force per unit volume can be expressed as [25,30] …”
Section: Interphase Momentum Transfermentioning
confidence: 99%