1982
DOI: 10.1007/bf00906109
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Breakup of droplets in turbulent shear flow of dilute liquid-liquid dispersions

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Cited by 9 publications
(6 citation statements)
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“…(9) Fig.1. The character of experimental data of the droplets breakup in pipelines [11] Droplets fragmentation mode: a) Identification of models of transfer processes 1157 However, as a result of size measurements of breakup resistant droplets in a pipeline with a diameter of 0.038 m Sleicher [5] found a completely different relation on the averaged flow rate:…”
Section: Alexander K Rozentsvaig and Cheslav S Strashinskiimentioning
confidence: 99%
“…(9) Fig.1. The character of experimental data of the droplets breakup in pipelines [11] Droplets fragmentation mode: a) Identification of models of transfer processes 1157 However, as a result of size measurements of breakup resistant droplets in a pipeline with a diameter of 0.038 m Sleicher [5] found a completely different relation on the averaged flow rate:…”
Section: Alexander K Rozentsvaig and Cheslav S Strashinskiimentioning
confidence: 99%
“…Rozentsvaig (1981) pointed out that the contribution of viscous shear may be significant to droplet breakage in pipe flows, and he modified the model in an attempt to reconcile it with the published experimental data. There is evidence that this particular power law form is not applicable in low-energy flows and some pipe flows (which are neither isotropic nor homogeneous).…”
Section: Droplet Breakagementioning
confidence: 99%
“…It would be incorrect to interpret the result using a simple additive model. A more general procedure for inclusion in inertial mechanism associated deformation gradient droplets is needed (Rozentsvaig [9]). …”
Section: (5) (6)mentioning
confidence: 99%
“…The quantitative effect of droplets deformation of inhomogeneous turbulence (6), which is complementary to relation for the inertial mechanism (5), is estimated using the constant α [9]:…”
Section: (5) (6)mentioning
confidence: 99%
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