Abstract

In the present work, we study the flow of thixotropic yield stress fluids between two concentric cylinders. In order to take into account the thixotropy, the constitutive relation uses a structural parameter which is driven by a kinetic equation. Here, the Houska's model is considered. Depending on the breakdown rate of the structural parameter, localization or shear-banding are observed. We show that for fragile structures, a shear-banding flow may be observed although for stronger structures, only localisation of the flow is observed such as in Bingham fluids. Physical explanations of the shear-banding discussed by several authors in the literature highlight that the shear-banding may be associated with a discontinuity into the structure of the material and a non-monotonic evolution of the stress according to the constitutive relation with the strain rate. Solving numerically the flow, we show that such a rheological model based on the existence of a structural parameter is able to predict shear-banding. Moreover, the consequences of the thixotropy on the linear stability of the azimuthal flow is studied in a large range of parameters. Although the thixotropy allows shear banding for the base flow, it does not modify fundamentaly the stability of the Couette flow compared to a simple yield stress fluid. The apparent shear-thinning behaviour depends on the thixotropic parameters of the fluid and the results about the onset of the Taylor vortices in shear-thinning fluids are retrieved. Nevertheless, the shear-banding modifies the stratification of the viscosity in the flowing zone such that the critical conditions are mainly driven by the width of the flowing region.

Highlights

  • Yield stress fluids, such as emulsions, foams, mud, and gels, are of industrial interest

  • We study of the stability of a thixotropic yield stress fluid in a Taylor-Couette configuration

  • The results found by Landry et al [2] with Bingham fluids or Alibenyahia et al [3] with shear-thinning fluids

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Summary

INTRODUCTION

Yield stress fluids, such as emulsions, foams, mud, and gels, are of industrial interest. We study of the stability of a thixotropic yield stress fluid in a Taylor-Couette configuration. In this article we use Houška’s model [9,10] It is built from the Hershel-Bulkley model, commonly used for nonelastic yield stress fluids, considering that the consistency K and the yield stress τ0 depend linearly on the structural parameter λ. This robust thixotropic fluid model was originally developed to characterize liquid foods such as ketchup or yogurt [9,10,11]. The linear stability analysis of the flow shows that the nature of the linear unstable mode is steady and axisymmetric in the large range of the explored parameters and does not depend on the thixotropic character of the flow

Flow geometry
Houška’s model
Nondimensional equations
Boundary conditions for the flow
Numerical methods for steady flows
EFFECT OF THE THIXOTROPY ON THE BASE FLOW
Steady-state flow curves
Velocity profiles and structural parameter
Interface between the static and the flowing regions
Equation setup
Convergence test and validation
Stability analysis of Couette flow of thixotropic yield stress fluids
REFERENCE VISCOSITY AND REFERENCE YIELD STRESS
Findings
CONCLUSION
Full Text
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