Intensification of mixing of shear-thinning fluids possessing yield stress with the coaxial mixers composed of two different central impellers and an anchor

2017 ◽  
Vol 111 ◽  
pp. 101-114 ◽  
Author(s):  
Argang Kazemzadeh ◽  
Farhad Ein-Mozaffari ◽  
Ali Lohi ◽  
Leila Pakzad
Keyword(s):  
Yield Stress ◽  
Shear Thinning ◽  
Shear Thinning Fluids ◽  
Coaxial Mixers

scholarly journals Mixing of shear-thinning fluids with yield stress in stirred tanks

AIChE Journal ◽  
2006 ◽  
Vol 52 (7) ◽  
pp. 2310-2322 ◽  
Author(s):  
P. E. Arratia ◽  
J. Kukura ◽  
J. Lacombe ◽  
F. J. Muzzio
Keyword(s):  
Yield Stress ◽  
Shear Thinning ◽  
Stirred Tanks ◽  
Shear Thinning Fluids

scholarly journals Droplet splashing during the impact on liquid pools of shear-thinning fluids with yield stress

2021 ◽  
Vol 33 (11) ◽  
pp. 112106
Author(s):  
Xiaoyun Peng ◽  
Tianyou Wang ◽  
Kai Sun ◽  
Zhizhao Che
Keyword(s):  
Yield Stress ◽  
Shear Thinning ◽  
Shear Thinning Fluids ◽  
Liquid Pools ◽  
The Impact

scholarly journals Concentric cylinder viscometer flows of Herschel-Bulkley fluids

2019 ◽  
Vol 29 (1) ◽  
pp. 173-181 ◽  
Author(s):  
Hans Joakim Skadsem ◽  
Arild Saasen
Keyword(s):  
Shear Rate ◽  
Yield Stress ◽  
Couette Flow ◽  
Newtonian Fluid ◽  
Shear Thinning ◽  
Newtonian Fluids ◽  
Drilling Fluids ◽  
Concentric Cylinder ◽  
Shear Thinning Fluids ◽  
Cylinder Viscometer

Abstract Drilling fluids and well cements are example non-Newtonian fluids that are used for geothermal and petroleum well construction. Measurement of the non-Newtonian fluid viscosities are normally performed using a concentric cylinder Couette geometry, where one of the cylinders rotates at a controlled speed or under a controlled torque. In this paper we address Couette flow of yield stress shear thinning fluids in concentric cylinder geometries.We focus on typical oilfield viscometers and discuss effects of yield stress and shear thinning on fluid yielding at low viscometer rotational speeds and errors caused by the Newtonian shear rate assumption. We relate these errors to possible implications for typical wellbore flows.

The Flow and Decay Behavior of a Submerged Shear-Thinning Jet With Yield Stress

2016 ◽  
Vol 138 (8) ◽  
Author(s):  
Khaled J. Hammad
Keyword(s):  
Yield Stress ◽  
Numerical Solutions ◽  
Shear Thinning ◽  
Momentum Conservation ◽  
Recirculation Region ◽  
Centerline Velocity ◽  
Flow Recirculation ◽  
Shear Thinning Fluids ◽  
Submerged Jets ◽  
The Impact

The flow and decay characteristics of submerged jets of shear-thinning fluids with yield stress are studied. Numerical solutions to the governing mass and momentum conservation equations, along with the Herschel–Bulkley rheological model, are obtained using a finite-difference scheme. A parametric study is implemented to investigate the influence of flow inertia and rheology over the following range of parameters: Reynolds number, 50 ≤ Re ≤ 200; yield number, 0 ≤ Y ≤ 1; and shear-thinning index, 0.6 ≤ n ≤ 1. A large recirculation region exists for Newtonian and shear-thinning non-Newtonian jets. However, the extent and strength of the recirculation region substantially diminish with the yield number and, to a lesser extent, when the shear-thinning index is reduced from 1 to 0.6. Increasing the yield number beyond a critical value eliminates flow recirculation. The centerline velocity and momentum decay of shear-thinning jets with yield stress, in general, increase with the yield number. Velocity- and momentum-based depths of penetration, DPU, and DPM, respectively, are introduced and presented. DPU and DPM are the downstream locations corresponding to 90% decay in the initial centerline velocity and jet momentum, respectively. A substantial decrease in DPU and DPM is observed when the shear-thinning index is reduced from 1 to 0.6 for Y = 0. The presence of yield stress significantly reduces both DPU and DPM of submerged jets. The impact of shear-thinning on the decay characteristics of the jet is more pronounced at low yield numbers.

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