“…The shear strength effect arises from interactions between small suspended 9 particles, which produce microstructures (e.g. Marangoni and Rogers 2003;Laxton and Berg 2006;Coussot et a!. 1993).…”
Section: Theorymentioning
confidence: 99%
“…Flow is laminar-like and confined between static regions when complex fluids are in transition from a quiescent state (Coussot et al 1993). The two-dimensional viscoplastic foam (Princen 1983) is often used as an analog for flowing condensed matter (Morral and Ashby 1974), particularly following an hexagonal array geometry (Khan and Armstrong 1986;Kem et al 2004;Cantat and Delanney 2005).…”
Non-Newtonian rheology is typical for the high-level radioactive waste (HLW) slurries processed in the Hanford Tank Waste Treatment and Immobilization Plant (WTP). Hydrogen and other flammable gases are generated in the aqueous phase by radiolytic and chemical reactions. HLW slurries have a capacity for retaining gas characterized by the shear strength holding the bubbles still. The sizes and degassing characteristics of flammable gas bubbles in the HLW slurries expected to be processed by the WTP are important considerations for designing equipment and operating procedures. Slurries become increasingly susceptible to degassing as the bubble concentration increases. This susceptibility and the process of ebullitive bubble enlargement are described here. When disturbed, the fluid undergoes localized flow around neighboring bubbles which are dragged together and coalesce, producing an enlarged bubble. For the conditions considered in this work, bubble size increase is enough to displace the weight required to overcome the fluid shear strength and yield the surroundings. The buoyant bubble ascends and accumulates others within a zone of influence, enlarging by a few orders of magnitude. This process describes how the first bubbles appear on the surface of a 7 Pa shear strength fluid a few seconds after being jarred.
“…The shear strength effect arises from interactions between small suspended 9 particles, which produce microstructures (e.g. Marangoni and Rogers 2003;Laxton and Berg 2006;Coussot et a!. 1993).…”
Section: Theorymentioning
confidence: 99%
“…Flow is laminar-like and confined between static regions when complex fluids are in transition from a quiescent state (Coussot et al 1993). The two-dimensional viscoplastic foam (Princen 1983) is often used as an analog for flowing condensed matter (Morral and Ashby 1974), particularly following an hexagonal array geometry (Khan and Armstrong 1986;Kem et al 2004;Cantat and Delanney 2005).…”
Non-Newtonian rheology is typical for the high-level radioactive waste (HLW) slurries processed in the Hanford Tank Waste Treatment and Immobilization Plant (WTP). Hydrogen and other flammable gases are generated in the aqueous phase by radiolytic and chemical reactions. HLW slurries have a capacity for retaining gas characterized by the shear strength holding the bubbles still. The sizes and degassing characteristics of flammable gas bubbles in the HLW slurries expected to be processed by the WTP are important considerations for designing equipment and operating procedures. Slurries become increasingly susceptible to degassing as the bubble concentration increases. This susceptibility and the process of ebullitive bubble enlargement are described here. When disturbed, the fluid undergoes localized flow around neighboring bubbles which are dragged together and coalesce, producing an enlarged bubble. For the conditions considered in this work, bubble size increase is enough to displace the weight required to overcome the fluid shear strength and yield the surroundings. The buoyant bubble ascends and accumulates others within a zone of influence, enlarging by a few orders of magnitude. This process describes how the first bubbles appear on the surface of a 7 Pa shear strength fluid a few seconds after being jarred.
“…Il est cependant possible, avec ces rhéomètres, de tester le mélange eau-argile interstitiel des laves. Mais même dans ce cas relativement simple les expériences doivent être réalisées avec beaucoup de précautions pour obtenir des résultats qui représentent effectivement la loi de comportement du fluide [7,10,14,25]. Les mélanges qui nous concernent font en effet partie de la grande classe des fluides à seuil qui posent de nombreux problèmes expé-rimentaux [26][27] et font encore l'objet de quelques débats conceptuels dans le domaine de la rhéologie.…”
Section: Détermination Des Paramètres Rhéologiquesunclassified
“…The current view of this research area, which we share, of the yield stress as a very viscous transition remains an attractive and useful engineering idea, and that it is a result of a network microstructure generated by inter-particle interactions, which may rupture into smaller clusters by large enough applied stresses and 15 then restores at a low stress level. The network needs time to build up and to disintegrate, and the rheology of the mixture therefore has a time scale; this results in a macroscopic thixotropic and yield stress behaviour, which has been considered one of the most complex phenomena in rheology [1]. For example, in cohesive sediment mixtures, which provide the motivation of this work, clay 20 particles flocculate and then break up under flow conditions.…”
Section: Introductionmentioning
confidence: 99%
“…exhibit a stable solid form at rest, and liquify once subjected to an applied stress exceeding a critical value -a yield-stress behaviour. This can be qualitatively explained by the forming and destruction of the fluid microstructure [1], and it may be modelled as a thixotropic and yield stress material. In this paper, we propose a mesoscopic model which is able to mimic a thixotropic and yield stress behaviour using a particle-based technique known as dissipative particle dynamics (DPD).…”
Many materials (e.g., gels, colloids, concentrated cohesive sediments, etc.) exhibit a stable solid form at rest, and liquify once subjected to an applied stress exceeding a critical value -a yield-stress behaviour. This can be qualitatively explained by the forming and destruction of the fluid microstructure [1], and it may be modelled as a thixotropic and yield stress material. In this paper, we propose a mesoscopic model which is able to mimic a thixotropic and yield stress behaviour using a particle-based technique known as dissipative particle dynamics (DPD). The DPD technique satisfies conservation of mass and momentum and it has been applied successfully for a number of problems in-
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