Hostname: page-component-6898cfcb55-w5hgh Total loading time: 0 Render date: 2026-11-11T08:30:02.882Z Has data issue: false hasContentIssue false

Modulation of elasto-inertial transitions in Taylor–Couette flow by small particles

Published online by Cambridge University Press:  27 October 2021

Tom Lacassagne*
Affiliation:
FLUME, Department of Mechanical Engineering, University College London (UCL), London WC1E 7JE, UKIMT Nord Europe, Institut Mines-Télécom, Univ. Lille, Centre for Energy en Environment, F-59000 Lille, France
Theofilos Boulafentis
Affiliation:
FLUME, Department of Mechanical Engineering, University College London (UCL), London WC1E 7JE, UK
Neil Cagney
Affiliation:
School of Engineering and Materials Science, Queen Mary University of London, London E1 4NS, UK
Stavroula Balabani*
Affiliation:
FLUME, Department of Mechanical Engineering, University College London (UCL), London WC1E 7JE, UK
*
†Email addresses for correspondence: tom.lacassagne@imt-nord-europe.fr, s.balabani@ucl.ac.uk
†Email addresses for correspondence: tom.lacassagne@imt-nord-europe.fr, s.balabani@ucl.ac.uk

Abstract

Particle suspensions in non-Newtonian liquid matrices are frequently encountered in nature and industrial applications. We here study the Taylor–Couette flow (TCF) of semidilute spherical particle suspensions (volume fraction $\leq 0.1$) in viscoelastic, constant-viscosity liquids (Boger fluids). We describe the influence of particle load on various flow transitions encountered in TCF of such fluids, and on the nature of these transitions. Particle addition is found to delay the onset of first- and second-order transitions, thus stabilising laminar flows. It also renders them hysteretic, suggesting an effect on the nature of bifurcations. The transition to elasto-inertial turbulence (EIT) is shown to be delayed by the presence of particles, and the features of EIT altered, with preserved spatio-temporal large scales. These results imply that particle loading and viscoelasticity, which are known to destabilise the flow when considered separately, can on the other hand compete with one another and ultimately stabilise the flow when considered together.

Information

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

Figure 1.Steady-shear dynamic viscosities $\mu$ for particle-loaded solvent and particle-loaded Boger fluid, for all three values of $\phi$, together with systematic characterisations of particle-free solvent and Boger matrix. Vertical dashed lines are plotted at $Wi=100$.

Figure 1

Table 1.Summary of experimental parameters for ramp-up (RU) and ramp-down (RD) experiments. Here $N_{RU}$ and $N_{RD}$ correspond to the number of repeated experiments for RU and RD, respectively, and $\varGamma _0={\mathrm {d}{Re}}/{\mathrm {d}t^*}=({\rho ^2 r_i d^3}/{\mu ^2})({\mathrm {d}\varOmega }/{\mathrm {d}t})$ is the non-dimensional acceleration rate, with $t^*=t/t_v$ the time scaled by the viscous time scale $t_v=\rho d^2/\mu$.

Figure 2

Figure 2.Schematic of the experimental set-up showing the Taylor–Couette cell, visualisation arrangement, and flow map construction. PC, personal computer; LED, light-emitting diode.

Figure 3

Figure 3.Example of RU (a,b), STS (c,d) and RD experiments (f,g) for a $\phi =0.1$ fluid (false colours). Panels (a,f) are $Re$-space diagrams (flow maps), (b,g) are frequency maps, (c,d) are space–time diagrams at fixed $Re$ and (e) shows temporal spectra extracted from the (b) frequency map at $Re$ corresponding to (c) and (d). Horizontal dashed lines in (b) and (g), and vertical dashed lines in (e) denote elastic wave frequencies $f^k=k\times f_e$ with $k=[\frac {1}{3},\frac {2}{3}]$ and $k=[\frac {1}{2},1]$ for the two first peaks in RU (b,e) and RD (g), respectively. Here, z is the location along the vertical axis and $f_{max}$ the maximum inner cylinder rotation frequency.

Figure 4

Figure 4.Critical $Re$–$\phi$ maps for transitions to TVF, RSW, EIT and SVF in RU (a) and RD (b) experiments. Hysteretic behaviours are illustrated for transitions to/from EIT, RSW and TVF in panels (ci, cii and ciii), respectively (triangles pointing upwards for RU, downwards for RD).

Figure 5

Figure 5.Illustration of the SVF state for RD experiments at $\phi =0.1$, on the flow map (a) and frequency map (c) (focus from figure 3f and 3g). Vertical dotted lines highlight transitions from RSW, RSW$+$SVF, SVF and CF from right to left (decreasing $Re$). A close-up of the flow map in the coexisting state range RSW$+$SVF is provided in panel (b) ($Re$ axis ranging from 118 to 136, $z/d$ axis from 5 to 20).

Figure 6

Figure 6.Two dimensional FFTs (time and space) of STS experiments for $\phi =0.01$ (a,b) and $\phi =0.1$ (c,d). Top left and top right parts on each panel display mean spectra in the frequency and space dimensions, respectively. The spatial wavelength axis is scaled by the gap size $d$ and the temporal frequency axis by $1/t_e$.