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Shear thickening in dense suspensions driven by particle interlocking

Published online by Cambridge University Press:  16 September 2022

Matthew Blair
Affiliation:
School of Engineering, University of Edinburgh, Edinburgh EH9 3JL, UK
Christopher Ness*
Affiliation:
School of Engineering, University of Edinburgh, Edinburgh EH9 3JL, UK
*
†Email address for correspondence: chris.ness@ed.ac.uk

Abstract

The processing of dense suspensions is a crucial step in many industries including mining; the production of ceramics; and the manufacture of pharmaceuticals. It is widely reported that these suspensions exhibit nonlinear behaviours such as shear thinning and thickening, with particle surface contacts recently being accepted as a primary culprit in the latter. In light of this, the modelling community have started to explore the role of particle surface tribology, predominantly by incorporating Coulombic friction models borrowed from the field of dry granular matter. Full details of the interactions between particle surfaces remain unclear, however, and it is suggested that physical interlocking of particle asperities may be key. Here, we use particle-based simulations to explore explicitly the effect of interlocking on the rheology of dense suspensions of micron-sized solids in a Newtonian fluid. Our simplified model recovers shear thinning, thickening and jamming phenomena commonly seen in experiments.

Information

Type
JFM Papers
Creative Commons
Creative Common License - CCCreative Common License - BY
This is an Open Access article, distributed under the terms of the Creative Commons Attribution licence (http://creativecommons.org/licenses/by/4.0), which permits unrestricted re-use, distribution and reproduction, provided the original article is properly cited.
Copyright
© The Author(s), 2022. Published by Cambridge University Press.
Figure 0

Figure 1.Schematic of aggregate particles (coloured by particle). Shown are suspensions with asperity sizes $k_r=$ (a) $0.05$; (b) $0.10$; (c) $0.20$. Green arrows indicate the imposed velocity profile $u_x(y) = \dot {\gamma }y$. Blue dashed circle represents contact with $P=0$ (see (3.1)).

Figure 1

Figure 2.Divergence of the relative viscosity $\eta _r$ with area fraction $\phi$ at $\dot {\gamma }^*=\infty$ for each of the suspension types explored. Shown in dashed lines are fits to $\eta _r = \nu (1-\phi /\phi _m)^{-\lambda }$. The maximum solid fractions for smooth particles $\mu =(0,100)$ and aggregates with $k_r=(0.05,0.10,0.20)$ are, respectively, $\phi _m=(0.84,0.77,0.74,0.71,0.69)$ (see table 1).

Figure 2

Table 1.Fitting parameters for the relative suspension viscosity as a function of the solid fraction, with functional form $\eta _r = \nu (1-\phi /\phi _m)^{-\lambda }$.

Figure 3

Figure 3.Rheology of smooth and aggregate particles, showing the relative viscosity $\eta _r$ as a function of shear rate $\dot {\gamma }^*$ (a,c,e,g,i) and stress $\eta _r\dot {\gamma }^*$ (b,d,f,h,j) for several $\phi$ (see legends). Shown are: (a,b) smooth frictionless ($\mu =0$) particles; (c,d) smooth frictional ($\mu =100$) particles; (e,f) aggregates with $k_r=0.05$; (g,h) aggregates with $k_r=0.10$; (i,j) aggregates with $k_r=0.20$. For (a–d) $\rho =0.1(a_i+a_j)$; for (e–j) $\rho =3k_ra_h$. Insets show sketches of smooth and aggregate particles represented in each panel.

Figure 4

Figure 4.Rheology of smooth and aggregate particles, showing the relative viscosity $\eta _r$ as a function of repulsive force decay rate $\rho$ (see legend). In each case the solid fraction $\phi$ is chosen close to frictional jamming, so that $\phi /\phi _m\approx 0.93$. Shown are: (a) smooth frictionless ($\mu =0$) particles; (b) smooth frictional ($\mu =100$) particles; (c) aggregates with $k_r=0.05$; (d) aggregates with $k_r=0.10$; (e) aggregates with $k_r=0.20$. Insets show sketches of smooth and aggregate particles represented in each panel.

Figure 5

Figure 5.Mechanical coordination number $Z$ for smooth and aggregate particle suspensions. (a) Sketches of the relative particle positions for various values of the interdigitation fraction $P$; (b) The coordination number measured by different criteria of interlocking, for particles with $k_r=0.20$, $\phi =0.62$ and $\rho =3k_ra_h$; (c) The coordination number ($Z, Z_{0.5}$) measured at different $\phi$ for smooth and aggregate particles (isostatic points depicted by arrows).

Figure 6

Figure 6.Mechanical coordination number as a function of dimensionless shear stress $(\eta _r\dot {\gamma }^*)$ at various solid fractions $\phi$. (a) Smooth particles with $\mu =0$; (b) smooth particles with $\mu =100$; (c) aggregates with $k_r=0.05$; (d) aggregates with $k_r=0.10$; (e) aggregates with $k_r=0.20$. For (a,b) $\rho =0.1(a_i+a_j)$; for (c–e) $\rho =3k_ra_h$ and we use $Z_{0.5}$. Insets show sketches of smooth and aggregate particles represented in each panel.

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