Knut Sverdrup - Google Scholar
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We find conditions that guarantee such motionless regimes and investigate flow development between static and advective states. Considering three problems, we explore the various ways in which the yield Some examples of viscoplastic fluids are mud, cement, lava, and paint. The constitutive models most often used to describe a viscoplastic fluid are the Bingham con-stitutive model [1] or the slightly more general Herschel-Bulkley constitutive model (2.8)-(2.9). The deformation and flow behavior of viscoplastic fluids can be realistically represented with the Herschel-Bulkley constitutive equation, which we have utilized as the basis for the development Thixotropic elasto-viscoplastic model for structured fluids P. R. de Souza Mendes, Soft Matter , 2011, 7 , 2471 DOI: 10.1039/C0SM01021A Here, analytical solutions are developed for the constant‐speed squeezing flow of viscoplastic fluids.
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[“Pressure-driven lubrication flow of a Bingham fluid in a channel: A novel approach” J. Non-Newtonian Fluid Mech. 221, 66–75 (2015)] and Panaseti et al. [“Pressure-driven flow of a Herschel-Bulkley fluid with pressure-dependent rheological parameters,” Phys. Fluids 30, 030701 (2018)], we write the momentum equation of the unyielded domain in an integral form Viscoplastic flow equationsFor non-Newtonian fluids, the viscosity is considered as a nonlinear function of the second invariant ( d ) of the rate-of-strain tensor (d ij ). A Bingham material remains rigid when the shear-stress is below the yield stress τ 0 , (here, equivalent to the Bingham number, Bn, as in Mitsoulis 2007), but flows like a Newtonian fluid when the shear-stress exceeds τ 0 . Fluids with yield stress (viscoplastic fluids) are commonly investigated using the Papanastasiou model 31: (1) Here, M is the stress growth parameter, t 0 is the yield stress, is shear‐rate, and η is fluid viscosity. In Stokes flow of a particle settling within a bath of viscoplastic fluid, a critical resistive force must be overcome in order for the particle to move.
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Authors Dimakopoulos Y., Tsamopoulos J. Abstract We study the transient displacement of Newtonian and viscoplastic liquids by highly pressurized air in cylindrical tubes of finite length with an expansion followed by … We present an experimental and numerical study of the turbulent displacement of viscoplastic fluids in a horizontal eccentric annulus. Several experiments where a weighted Newtonian fluid displaces a yield stress fluid under a turbulent flow condition are presented and discussed. 8:30-8:45 Mesoscopic Model for Bingham Fluids and Mixed Convection Flows in a Lid Driven Cavity (Part I) R.R. Huilgol 8:45-9:00 Mesoscopic Model for Bingham Fluids and Mixed Convection Flows in a Lid Driven Cavity (Part II) R.R. Huilgol 9:00-9:15 Morphology of drop impact onto a viscoplastic … Rayleigh-Bénard convection for viscoplastic fluids. 2011.
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Drilling fluid is conventionally modeled using power law parameters and yield stress. Examples of constitutive equations obtained using both procedures are presented. We show that irrespective of the method used, it is not possible to obtain consistent viscoplastic fluid formulations starting from certain yield functions. Comparisons between the response of the proposed models for uniaxial compression conditions is provided. We experimentally study the viscous fingering problem of viscoplastic fluids in channels of rectangular cross section. We find that a yield stress-dependent capillary number (${\text{Ca}}^{*}$) and an aspect ratio-dependent Bond number (${\text{Bo}}^{*}$) can classify the finger shape into ramified and unified fingering patterns, and the finger flow regime into yield stress, viscosity, and Helical flow of viscoplastic Herschel‐Bulkley fluids in concentric and eccentric annuli with rotating inner cylinder was investigated numerically. Similar flows occur in drilling operations of oil and gas wells.
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New packaging technology has been introduced that will change how viscous liquids move throughout packaging, eliminating product waste withi. Filtration of high viscosity liquids or liquids with high solids content. Filtering liquid with a high viscosity or high solid content is fairly uncommon, especially
In wells it is caused by the mechanical friction within the drilling mud due to interaction between solids, the liquids and the deformation of liquid that is under shear
Viscoplastic Fluid Behavior Viscoplastic fluids behave as if they have a yield stress (t0). Until t0 is exceeded they do not appear to flow. A Bingham plastic fluid
29 Aug 2014 There are viscoelastic fluids, which have a very curious behavior.
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8:30-8:45 Mesoscopic Model for Bingham Fluids and Mixed Convection Flows in a Lid Driven Cavity (Part I) R.R. Huilgol 8:45-9:00 Mesoscopic Model for Bingham Fluids and Mixed Convection Flows in a Lid Driven Cavity (Part II) R.R. Huilgol 9:00-9:15 Morphology of drop impact onto a viscoplastic … Rayleigh-Bénard convection for viscoplastic fluids.
If the applied stress exceeds the yield stress, the material flows like a viscous fluid, typically featuring a nonlinear shear-dependent viscosity.
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PDF Modelling of constitutive and fatigue behaviour of a
Rayleigh and Marangoni convection and rheology are linked in the thermal convection of viscoelastic fluids to some recent technological applications. Such technology developments as the ones presented here undoubtedly shall be based on interdisciplinary projects involving not only rheology or fluid mechanics but several other disciplines. INTRODUCTION.
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Such behavior characterizes materials common in industries such as petroleum and chemical processing, cosmetics, and food processing and in geophysical fluid dynamics. The most common Some traditional viscoplastic materials in some non-traditional flow configurations, and some non-traditional viscoplastic fluid flows (plus pertinent references), from top right to bottom left A constitutive model for structured fluids is presented. Its predictive capability includes thixotropy, viscoelasticity and yielding behavior. It is composed by two differential equations, one for the stress and the other for the structure parameter—a scalar quantity that represents the structuring level of the fluid. Rayleigh-Bénard convection for viscoplastic fluids @article{Darbouli2011RayleighBnardCF, title={Rayleigh-B{\'e}nard convection for viscoplastic fluids}, author={Mohamed Darbouli and Christel M{\'e}tivier and J. Piau and A. Magnin and Ahmed Abdelali}, journal={Physics of Fluids}, year={2011}, volume={25}, pages={023101} } An important class of non-Newtonian fluids presents a yield stress limit which must be exceeded before significant deformation can occur – the so-called viscoplastic fluids or Bingham plastics.