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Herschel–Bulkley fluid

About: Herschel–Bulkley fluid is a research topic. Over the lifetime, 1946 publications have been published within this topic receiving 49318 citations.


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Journal ArticleDOI
TL;DR: In this article, a non-orthogonal stagnation flow of an Oldroyd-B fluid between two parallel plates is considered and the problem is reduced to a set of ODEs, which are then solved with finite differences using a parameter continuation method.
Abstract: This paper is concerned with a non-orthogonal stagnation flow of an Oldroyd-B fluid between two parallel plates. We reduce the problem to a set of ordinary differential equations (ODE's), which is then solved with finite differences using a parameter continuation method. Perturbation analyses are also carried out for small Reynolds numbers and small Weissenberg numbers respectively. The solution of the set of ODE's is discussed. It is known that for a Newtonian fluid, the stagnation point shifts from the potential flow case in the opposite direction of the tangential velocity. The effect of the fluid elasticity is to reduce this shift. It is also shown that the Oldroyd-B model has a limiting Weissenbeg number, depending on the angle of the injected flow.

8 citations

Journal Article
TL;DR: In this paper, the flow behavior of pressure and temperature-treated α-lactalbumin dispersions was studied using a controlled rate rheometer, and the shear stress-shear rate data were described with the Herschel Bulkley model with yield stress.
Abstract: The flow behavior of pressure and temperature-treated α-lactalbumin dispersions was studied using a controlled rate rheometer. Dispersions 10% (w/w) of α-lactalbumin were subjected to high hydrostatic pressure from 100 MPa to 400 MPa at 20°C for 30 min or thermal treatment from 20°C to 80°C for 15 min at atmospheric pressure, followed by rheological characterisation at shear rates between O/s and 200/s. The shear stress-shear rate data of both pressure and heat-treated α-lactalbumin dispersions were described with the Herschel Bulkley model with yield stress. Dispersions exhibited shear-thinning behavior with flow behavior indices less than unity. Hydrostatic pressure treatment of α-lactalbumin samples did not change the magnitude of rheological parameters (p>0.05) and there was no gel formation. Consistency coefficient and apparent viscosity at 100/s decreased linearly with temperature and followed the Arrhenius relationship. The flow activation energy was found to be 10.18 kJ/mol and 11.57 kJ/mol for consistency index and apparent viscosity, respectively. Lower flow activation energy signified lesser molecular interaction or denaturation of protein molecules during thermal treatment of α-lactalbumin.

8 citations

Journal ArticleDOI
TL;DR: In this article, the authors solved the problem of creeping flow past a sphere for a limiting case of fluid behaviour: an abrupt change in viscosity, and solved it for the case where the fluid is smooth.
Abstract: Creeping flow past a sphere is solved for a limiting case of fluid behaviour: an abrupt change in viscosity.

7 citations

Journal ArticleDOI
TL;DR: An exact solution for the flow of an elastico-viscous fluid (Walters' liquid B') due to an oscillating infinite plate has been derived in this paper, where it has been observed that the flow near the plate may become unstable with increasing ω whereas for ωt>0, the velocity increases with increasingω.
Abstract: An exact solution for the flow of an elastico-viscous fluid (Walters' liquid B') due to an oscillating infinite plate has been derived. It has been observed that forgwt=0, (ω — frequency,t — time) the flow near the plate may become unstable with increasing ω whereas forωt>0, the velocity increases with increasingω. The shearing stress decreases with increasingω.

7 citations

01 Jan 2014
TL;DR: In this paper, a closed model for the averaged viscosity that takes into account its nonlinear dependence on the fluctuating rate of deformation tensor is proposed. But the model is based on the Reynolds-Averaged approach.
Abstract: A novel turbulence model for flows of viscoplastic fluid is presented. It is based on the Reynolds-Averaged approach. A closed model for the averaged viscosity that takes into account its nonlinear dependence on the fluctuating rate of deformation tensor is proposed. Test calculations were performed for power-law fluid and Herschel–Bulkley fluid flows in a straight round pipe. Numerical data obtained with the use of the proposed model are compared with the results of direct numerical simulations. The proposed model adequately describes the reduction in the turbulent transport of momentum with decreasing power-law index and with increasing yield stress of the fluid.

7 citations


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Performance
Metrics
No. of papers in the topic in previous years
YearPapers
202341
202295
202117
202022
201920
201836