2018
DOI: 10.1122/1.4995348
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Rising bubbles in yield stress materials

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Cited by 44 publications
(67 citation statements)
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“…As the bubble grows, inertia forces grow and exceed the surface tension, which becomes negligible. These results are in contrast with the ones observed in the experimental study made by Sikorski et al (2009) and Lopez et al (2017), where it was observed bubble shapes with a rounded head and a cusped tail. How-ever, this difference can be due to elasticity that is present in the fluid used in the experiments.…”
Section: Fig 6 Wall Effect On Bubble Velocity For τY =contrasting
confidence: 99%
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“…As the bubble grows, inertia forces grow and exceed the surface tension, which becomes negligible. These results are in contrast with the ones observed in the experimental study made by Sikorski et al (2009) and Lopez et al (2017), where it was observed bubble shapes with a rounded head and a cusped tail. How-ever, this difference can be due to elasticity that is present in the fluid used in the experiments.…”
Section: Fig 6 Wall Effect On Bubble Velocity For τY =contrasting
confidence: 99%
“…5, where it is noted that the Reynolds number decreases with the Bingham number up to a certain value of Bn above which the force balance be-tween yield stress and buoyancy leads the bubble to remain stagnant. These results are in qualitative agreement with the ones obtained in Dimakopoulos et al (2013) and Lopez et al (2017). Fig.…”
Section: Single Bubblesupporting
confidence: 92%
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“…pastes, slurries, emulsions and microgels which possess a characteristic stress τ y below which they stop flowing and behave as solids [1,2]. They may trap bubbles when buoyancy-induced stresses do not suffice to yield the material [3][4][5][6][7][8][9][10][11].…”
Section: Introductionmentioning
confidence: 99%
“…Elastic effects can be observed also in the fluid phase. For example, bubbles rising in Carbopol solutions usually acquire the shape of an inverted teardrop, with a cusp at their leeward side [13,14], but the classical Bingham and HB viscoplastic models fail to predict such behaviour [15,16]; on the other hand, such shapes are observed also in viscoelastic fluids, and are correctly captured by viscoelastic constitutive equations [17]. Similarly, for the settling of spherical particles in Carbopol, classical VP models cannot predict phenomena such as the loss of fore-aft symmetry under creeping flow conditions and the formation of a negative wake behind the sphere, but these phenomena are predicted if elasticity is incorporated into the constitutive modelling [18].…”
Section: Introductionmentioning
confidence: 99%