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Prediction of shear thickening of particle suspensions in viscoelastic fluids by direct numerical simulation

Published online by Cambridge University Press:  01 March 2021

Yuki Matsuoka*
Affiliation:
Corporate Engineering Center, Sumitomo Bakelite Co. Ltd, Shizuoka 426-0041, JapanDepartment of Chemical Engineering, Kyushu University, Fukuoka 819-0395, Japan
Yasuya Nakayama*
Affiliation:
Department of Chemical Engineering, Kyushu University, Fukuoka 819-0395, Japan
Toshihisa Kajiwara
Affiliation:
Department of Chemical Engineering, Kyushu University, Fukuoka 819-0395, Japan
*
†Email addresses for correspondence: ymatsuoka@sumibe.co.jp, nakayama@chem-eng.kyushu-u.ac.jp
†Email addresses for correspondence: ymatsuoka@sumibe.co.jp, nakayama@chem-eng.kyushu-u.ac.jp

Abstract

To elucidate the key factor for the quantitative prediction of the shear thickening in suspensions in viscoelastic fluids, direct numerical simulations of many-particle suspensions in a multi-mode Oldroyd-B fluid are performed using the smoothed profile method. Suspension flow under simple shear flow is solved under periodic boundary conditions by using Lees–Edwards boundary conditions for particle dynamics and a time-dependent oblique coordinate system that evolves with mean shear flow for fluid dynamics. Semidilute many-particle suspensions up to a particle volume fraction of 0.1 are investigated. The presented numerical results regarding the bulk rheological properties of the shear-thickening behaviour agree quantitatively with recent experimental results of semidilute suspensions in a Boger fluid. The presented result clarifies that an accurate estimation of the first normal stress difference of the matrix in the shear-rate range where the shear thickening starts to occur is crucial for the quantitative prediction of the suspension shear thickening in a Boger fluid matrix at around the Weissenberg number ${Wi}=1$ by an Oldroyd-B model. Additionally, the effect of suspension microstructures on the suspension viscosity is examined. The paper concludes with a discussion on how the flow pattern and the elastic stress development change with the volume fraction and Weissenberg number.

Information

Type
JFM Papers
Copyright
© The Author(s), 2021. Published by Cambridge University Press
Figure 0

Figure 1.Schematic diagrams of the simulation set-up: (a) single-particle system and (b) the sliding cell interpretation of Lees–Edwards boundary conditions. Here $U_x=\dot {\gamma }r_y$ represents the velocity of the mean shear flow; and $L$ is the box length of the cubic domain. In (b), the image cells along the vorticity direction are not shown for simplicity.

Figure 1

Figure 2.The ${Wi}$ dependence of the relative viscosity of a dilute Oldroyd-B suspension at $\beta =0.5$. The inset shows the ${Wi}$ dependence of the thickening part of $\eta _r$. Red open circles represent results from this work. The black lines correspond to the theoretical prediction by Einarsson et al. (2018) using (3.1).

Figure 2

Figure 3.The ${Wi}$ dependence of (a) stresslet $\alpha _S^{{stresslet}}$ and (b) particle-induced fluid stress $\alpha _S^{{fluid}}$ contributions to the suspension viscosity at $\beta =0.5$. Red filled circles represent results from this work, and blue squares are the DNS results by Einarsson et al. (2018). The black line is plotted according to the theory by Einarsson et al. (2018).

Figure 3

Table 1.Parameters for a four-mode Oldroyd-B fluid. The values are from table 1 of Yang & Shaqfeh (2018b), which are estimated from the small-amplitude oscillatory shear measurement of a Boger fluid.

Figure 4

Figure 4.The $\phi _p$ dependence of the relative viscosity of suspensions at ${Wi}=0.1$ (blue circles), $0.5$ (green triangles), $1.0$ (orange squares) and $2.0$ (red diamonds). The short-dashed and long-dashed lines correspond to the theoretical predictions for a Newtonian suspension by Einstein (1911) and Batchelor & Green (1972), respectively. The empirical prediction from Haddadi & Morris (2014) is shown as a solid line.

Figure 5

Figure 5.Viscometric functions of suspensions as functions of ${Wi}$ and $\phi _p$: (a) relative viscosity and (b) relative first NSD coefficient of suspensions. The closed symbols are simulated results from this work, and the open symbols are experimental results from Yang & Shaqfeh (2018b). The blue squares, green triangles and red circles correspond to the results for $\phi _p=0.025$, 0.05 and $0.1$, respectively. Experimental $\eta _{r}$ and $\varPsi _{1,r}$ are calculated using $\eta (\phi _p, \dot {\gamma })$ and $\varPsi _{1}(\phi _p, \dot {\gamma })$ reported by Yang & Shaqfeh (2018b). The dashed lines in (a) are values predicted by the Eilers fit (Haddadi & Morris 2014). Solid lines are guides to the eye. The insets in (a,b) show the DNS results at $\phi _p=0.1$ by the multi-mode model (red circles) and the effective single-mode model (black squares) explained in § 3.2.3.

Figure 6

Figure 6.DNS results at $\phi _p=0.025$: (a) suspension viscosity for single-particle (red circles) and many-particle (blue squares) systems; and (b) microstructure in a many-particle system at ${Wi}=2.0$. In (a), the black lines are predictions for Newtonian suspensions according to the theories of Batchelor & Green (dashed) and Einstein (dot-dashed). Solid lines are guides to the eye.

Figure 7

Figure 7.Proportions of each relaxation mode in the polymer stress contribution (for $k=1$ (red circles), 2 (orange triangles), 3 (green squares) and 4 (blue diamonds), and the sum of the mode contributions (black downward-pointing triangles)): (a) shear viscosity and (b) first NSD coefficient at $\phi _p=0.1$. The values of $\langle \eta _{p}^{(k)}\rangle$ and $\langle \varPsi _{1,p}^{(k)}\rangle$ are normalized by $\eta _0$ and $\varPsi _1(\phi _p=0)=2\sum _{k=1}^4\eta _p^{(k)}\lambda ^{(k)}$, respectively. Note that the stresslet contributions are not included in the figure. Lines are guides to the eye. By definition, the order of $\langle \eta _{p}^{(k)}\rangle$ and $\langle \varPsi _{1,p}^{(k)}\rangle$ at ${Wi}\rightarrow 0$ corresponds to the order of $\eta _p^{(k)}$ and $\eta _p^{(k)}\lambda ^{(k)}$ in table 1, respectively. That is why $\langle \eta _{p}^{(4)}\rangle >\langle \eta _{p}^{(3)}\rangle$ in (a). In (b), $\langle \varPsi _{1,p}^{(4)}\rangle$ is not shown because it is smaller than $\langle \varPsi _{1,p}^{(3)}\rangle$.

Figure 8

Figure 8.Contributions to the total suspension stress from stresslet $\boldsymbol{\mathsf{S}}$ (red) and particle-induced fluid stress $\boldsymbol {\varSigma }$ (blue) at $\phi _p=0.001$ to 0.1 (from light to dark colour): (a) contributions to the total shear stress normalized by $\eta _0\dot {\gamma }a^3$; and (b) contributions to the total first NSD normalized by $\eta _0\lambda ^{(1)}\dot {\gamma }^2a^3$. Solid lines are guides to the eye.

Figure 9

Figure 9.Viscoelastic contributions to the total suspension shear stress as a function of the effective Weissenberg number at $\phi _p=0.001$ to 0.1 (from light to dark colour). (a) Stresslet contribution to shear stress. The ordinate represents the polymeric part of $\langle {\mathsf{S}}_{xy}\rangle$, i.e. $\langle {\mathsf{S}}_{xy}\rangle -\langle {\mathsf{S}}_{xy,0}\rangle$, where $\langle {\mathsf{S}}_{xy,0}\rangle$ is the Newtonian part of $\langle {\mathsf{S}}_{xy}\rangle$ represented by (3.4). The inset shows the $\phi _p$ dependence of $\langle {\mathsf{S}}_{xy}\rangle$ at ${Wi}=0.1$ (red circles). The result from single-particle simulation at $\phi _p=0.025$ is also shown (red square). The black lines are predictions according to theories of Einstein (dotted), Batchelor & Green (dot-dashed) and Eilers fit by Haddadi & Morris (solid). The contributions for the shear stress are normalized by $\eta _0\dot {\gamma }a^3$. (b) Particle-induced fluid stress contributions for shear stress. The effective Weissenberg number $\widetilde {{Wi}}$ is defined with the average strain rate in the fluid region at each $\phi _p$. In both panels, the red and blue solid lines are guides to the eye.

Figure 10

Figure 10.Viscoelastic contributions to the total suspension shear stress as a function of the suspension shear stress at $\phi _p=0.001$ to $0.1$ (from light to dark colour): (a) stresslet, (b) particle-induced fluid stress, (c) normalized polymer dissipation function of the first relaxation mode, and (d) the thickening portion of the relative viscosity. The suspension shear stress in the abscissa in each panel is non-dimensionalized as $\langle \sigma _{xy}^{{sus}}\rangle \lambda ^{(1)}/\eta _0$. Solid lines are guides to the eye.

Figure 11

Figure 11.The $\phi _p$ and ${Wi}$ dependence of the local strain rate in the fluid region. (a) P.d.f. of $\dot {\gamma }_{{local}}$, where $\phi _p=0.1$ (red), 0.05 (orange), 0.025 (green) and 0.001 (blue), and the dotted and solid lines represent p.d.f.s at ${Wi}=0.1$ and $2.0$, respectively. The strain rate is normalized by the imposed shear rate $\dot {\gamma }$, and the arrows indicate the first and second relaxation rates at ${Wi}=2.0$. The inset shows the $\phi _p$ dependence of the mean and standard deviation for $Wi=0.1$ (open symbols) and 2.0 (closed symbols). (b) P.d.f. of $\dot {\gamma }_{local}$ centred at the mean and normalized by the standard deviation. The inset shows the $\phi _p$ dependence of the skewness and kurtosis. The line types are the same as those in (a). The dashed line indicates the standard Gaussian distribution. (c) Average local strain rate, where blue squares and red circles correspond to $Wi=0.1$ and 2.0, respectively, and the line is the result from homogenization theory.

Figure 12

Figure 12.P.d.f. of (a) strain-rate state $s$ and (b) irrotationality $E$ in the fluid region at various values of $\phi _p$ (0.1 (red), 0.05 (orange), 0.025 (green) and 0.001 (blue)). For each $\phi _p$, ${Wi}=0.1$ (dotted lines) and 2.0 (solid lines). The inset shows the $\phi _p$ dependence of the mean (red circles) and standard deviation (blue squares). The open and solid symbols in the inset indicate the results of ${Wi}=0.1$ and $2.0$, respectively.

Figure 13

Figure 13.The 2-D p.d.f.s of strain-rate state $s$ and irrotationality $E$ in the fluid region: (a,b) $\phi _p=0.001$; (c,d) $\phi _p=0.025$; (e,f) $\phi _p=0.05$; and (g,h) $\phi _p=0.1$. The top and bottom rows indicate the results at ${Wi}=0.1$ and $2.0$, respectively. The contour lines correspond to $\textrm {p.d.f.}=10^k$ with $k=-4,-3,-2,-1,0,1,2$.

Figure 14

Figure 14.Spatial distribution of the flow pattern characterized by: (a,b) strain-rate state $s$; (c,d) irrotationality $E$; (e,f) normalized polymer stretch of the first mode $(\text {tr}\,\boldsymbol{\mathsf{C}}^{(1)}-3)/(2{Wi}^2)$; and (g,h) normalized shear stress of the first mode $\sigma _{p,xy}^{(1)}/(\eta _{p}^{(1)}\dot {\gamma })$ on a shear plane ($x,y$ plane) at ${Wi}=0.5$. The top (a,c,e,g) and bottom (b,d,f,h) rows are the results at $\phi _p=0.025$ and $0.1$, respectively.

Figure 15

Figure 15.Spatial distribution of the flow pattern characterized by: (a,b) strain-rate state $s$; (c,d) irrotationality $E$; (e,f) normalized polymer stretch of the first mode $(\text {tr}\,\boldsymbol{\mathsf{C}}^{(1)}-3)/(2{Wi}^2)$; and (g,h) normalized shear stress of the first mode $\sigma _{p,xy}^{(1)}/(\eta _{p}^{(1)}\dot {\gamma })$ on a shear plane ($x,y$ plane) at ${Wi}=2.0$. The top (a,c,e,g) and bottom (b,d,f,h) rows are the results at $\phi _p=0.025$ and $0.1$, respectively.

Figure 16

Figure 16.The isovolume visualization of a highly irrotational region at ${Wi}=2.0$: (a) $\phi _p=0.001$, (b) $0.025$, (c) $0.05$ and (d) $0.1$. The isovolume represents a region where $E\geqslant 0.65$, and the colour represents the strain-rate state $s$.

Figure 17

Figure 17.Polymer high-stretch region at ${Wi}=2.0$: (a) $\phi _p=0.025$, (b) $0.05$ and (c) $0.1$. The isovolume of $\textrm {tr}\,\boldsymbol{\mathsf{C}}^{(1)}\geqslant 2(2\widetilde {{Wi}}^2+3)$ is visualized in green, where the threshold is twice the value of $\text {tr}\,\boldsymbol{\mathsf{C}}$ in the Oldroyd-B fluid under homogeneous shear flow.

Figure 18

Figure 18.Schematic diagram of the oblique coordinate system. Here $\hat {\boldsymbol {E}}_1$ and $\hat {\boldsymbol {E}}_2$ and $\boldsymbol {e}_1$ and $\boldsymbol {e}_2$ are the basis vectors in the oblique system and those in the static Cartesian system, respectively; and $r^1$ and $r^2$ are the components of the position vector in the Cartesian system. The Cartesian system and the initial oblique system coincide (blue square). At $t>0$, the oblique system is sheared (pink parallelogram) by the strain of $\dot {\gamma }t$, where $\dot {\gamma }$ is the applied shear rate. The region of the oblique system outside the initial square (right triangle) can be periodically transformed back into the square (left triangle).

Figure 19

Figure 19.Flow chart of the main calculation procedure over one time step.

Figure 20

Figure 20.Mesh resolution dependence of polymer shear stress distributions near the particle. In panels (a–d) the polymer shear stress normalized by $\eta _p\dot {\gamma }$ on the shear plane through the centre of the particle is drawn by colour contour for $(a/\varDelta ,\xi /\varDelta )=(8,2)$, $(8,1)$ and $(20,2)$ and for the analytical solution, respectively. The dotted lines around the particles for the DNS results in panels (a–c) denote the radial location of $a+\xi /2$.(It may be necessary to zoom-in to see these.) In panel (e), the normalized polymer shear stress along the line from the particle centre to the shear gradient direction $y$ is drawn: the exact solution (analytical) of $\boldsymbol {\sigma }_p/(\eta _p\dot {\gamma }) \approx 2\tilde {\boldsymbol{\mathsf{D}}}-2{Wi}\tilde {\boldsymbol{\mathsf{D}}}_{(2)}$ at ${Wi}\to 0$ (solid line), and the results for $(a/\varDelta ,\xi /\varDelta )=(20,2)$ (red), $(8,2)$ (green) and $(8,1)$ (blue), respectively. In panel (e), the interface region indicated by $0<\phi <1$ at around $r_y/a=1$ with thickness $\xi$ is coloured in the same manner as that for the symbols.

Figure 21

Figure 21.The ${Wi}$ dependence of the normalized particle angular velocity $\omega _z/\dot {\gamma }$. (a) The result of this work (red circles) compared with a previous numerical result (solid line; Snijkers et al.2009) and the asymptotic solution (dashed line; Housiadas & Tanner 2011a,b, 2018) at $\beta =0.615$. (b) The $\beta$ dependence of $\omega _z/\dot {\gamma }$ for: $\beta =0.2$ (red circles), $0.5$ (orange squares), $0.615$ (green triangles) and $0.8$ (blue diamonds). The lines correspond to predictions of the asymptotic solution.

Figure 22

Figure 22.The ${Wi}$ dependence of the normalized energy dissipation around a particle at $\beta =0.5$: (a,b) ${Wi}=0.1$ and (c,d) ${Wi}=1.0$. Panels (a,c) and (b,d) show the distributions of viscous dissipation $\varPhi _{s}/(\eta _0\dot {\gamma }^2)$ and polymer dissipation $\varPhi _{p}/(\eta _0\dot {\gamma }^2)$, respectively. The dotted lines around particles show the radial location of $a+\xi /2$. (Again, it may be necessary to zoom-in to see these.)