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Intermittency and hibernation in elasto-inertial Taylor–Couette flow at moderate Reynolds number

Published online by Cambridge University Press:  23 October 2026

Theofilos Boulafentis
Affiliation:
Department of Mechanical Engineering, University College London, London WC1E 6BT, UK
Tom Lacassagne
Affiliation:
Institut Mines-Télécom, Univ. Lille, Centre for Energy and Environment, IMT Nord Europe, Lille F-59000, France
Neil Cagney
Affiliation:
School of Engineering and Materials Science, Queen Mary University of London, London E1 4NS, UK
Stavroula Balabani*
Affiliation:
Department of Mechanical Engineering, University College London, London WC1E 6BT, UK
*
Corresponding author: Stavroula Balabani, s.balabani@ucl.ac.uk

Abstract

Content of image described in text.

We investigate the presence of intermittency, a well-known phenomenon in Newtonian turbulence, in viscoelastic Taylor–Couette flow at fixed inertia, (Reynolds number, $\textit {Re}$ = 120). Using particle image velocimetry measurements in the r–z plane for a broad range of elasticities, $\textit{El}$ = 0–0.64, we reveal a dual role of viscoelasticity, even at moderate $\textit {Re}$: it can destabilise the flow and trigger turbulence at moderate elasticity but suppress turbulence intensity at higher values. Gradual turbulence suppression is evident through reduced velocity fluctuations, longer integral time scales proportional to the polymer relaxation time and weakened coherent structures as the flow approaches elasto-inertial turbulence. Higher-order statistics indicate that elasticity increases spatial and temporal intermittency while altering the dynamics: spatially, through a reduced viscous range and enhanced large-scale decorrelation; temporally, via a characteristic time scale consistent with polymer-driven state switching rather than a classical cascade. This spatio-temporal intermittency manifests as alternating active/hibernating turbulence cycles. During hibernation, the flow reorganises into a state distinct from active turbulence, characterised by low velocity fluctuations and Reynolds stresses, suppressing not only turbulence but also linearly unstable Newtonian states such as Taylor vortices. Rather than being featureless, this state exhibits weakened coherent structures in the bulk of the flow and sustained near-wall dynamics, where elastic stresses are likely generated. The present results demonstrate that hibernation is not exclusive to Newtonian turbulence, but also emerges in viscoelastic flows under conditions where inertia alone is insufficient to trigger or sustain turbulent motion.

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 (https://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), 2026. Published by Cambridge University Press
Figure 0

Table 1. A summary of the rheological properties of the fluids.Table 1 long description.

Figure 1

Figure 1. Figure 1 long description.Schematic representation of the TC cell and the particle image velocimetry (PIV) set-up.

Figure 2

Figure 2. Figure 2 long description.(a) Steady-shear rheological properties of the PAAM solutions used in this work for different concentrations, (b) filament diameter evolution for different PAAM concentrations. The solvent (WGL-80) is the same for all cases, 80 % glycerol and 20 % water.

Figure 3

Table 2. A summary of the experimental settings for the PIV experiments.Table 2 long description.

Figure 4

Figure 3. Figure 3 long description.Velocity vectors with azimuthal vorticity contours, normalised by the rotational speed of the inner cylinder, Ωθ/Ωi$\varOmega _{\theta }/\varOmega _i$, for fixed Reynolds number, Re$\textit {Re}$ = 120 and (a) Wi$\textit{Wi}$ = 0 (0 ppm), (b) Wi$\textit{Wi}$ = 2.3 (5 ppm), (c) Wi$\textit{Wi}$ = 8.3 (10 ppm), (d) Wi$\textit{Wi}$ = 40.2 (200 ppm) and (e) Wi$\textit{Wi}$ = 76.4 (700 ppm). The cross symbols in (a) and (b) show the approximate centres of the Taylor vortices.

Figure 5

Figure 4. Figure 4 long description.Spatio-temporal maps of the instantaneous radial velocities, ur$u_r$, for Wi$\textit{Wi}$ = 0–76.4. The velocities are averaged across the gap and are shown over a period of 5 s.

Figure 6

Figure 5. Figure 5 long description.(a) Average magnitude of radial velocities at the inflow (orange line), ur,in¯$\overline {u_{r,in}}$, and outflow (blue line), ur,out¯$\overline {u_{r,out}}$ boundaries for Wi$\textit{Wi}$ = 0–76.4. The values are normalised with the rotational speed of the inner cylinder Ωiri$\varOmega _ir_i$. The ratio of the two, R=ur,in¯/ur,out¯$R=\overline {u_{r,in}}/\overline {u_{r,out}}$, is also presented by the dotted black line. (b) Fast-Fourier transform (FFT) of the radial velocity fluctuations for Wi$\textit{Wi}$ = 0–76.4. (c) Maximum value of the root-mean-square of the radial velocity fluctuations of the original (black line) and filtered (yellow line) data, (d) azimuthal vorticity magnitude |Ωθ|$|\varOmega _{\theta }|$ (left axis) and magnitude of the root-mean-square of azimuthal vorticity fluctuations, |Ωθ,rms′|$|\varOmega '_{\theta ,rms}|$ (right axis), normalised by the rotational speed of the inner cylinder Ωi$\varOmega _i$. The error bars denote the standard deviation between different data sets, where available.

Figure 7

Figure 6. Figure 6 long description.(a) Fraction of the average area covered by vortical structures, Af$A_{\!f}$ and (b) probability density function (pdf) of the position of the vortical structures cores, for Wi$\textit{Wi}$ = 0–76.4.

Figure 8

Figure 7. Figure 7 long description.Contours of two-dimensional spatial correlation of radial velocity fluctuation, Cur′ (ξ)$C_{u'_r}\ (\boldsymbol{\xi })$ (a) and axial velocity fluctuations, Cuz′ (ξ)$C_{u'_z}\ (\boldsymbol{\xi })$ (b), for Wi$\textit{Wi}$ = 0, 2.3, 8.3, 14.5, 40.2, 63.7, 71, 76.4 (from top to bottom).

Figure 9

Figure 8. Figure 8 long description.Curves of Cur′ (ξz)$C_{u'_r}\ (\xi_z )$ averaged across the gap for Wi$\textit{Wi}$ = 0–76.4. The curves are shown in the range −2⩽ξz/d⩽2$-2\leqslant \xi _z/d \leqslant 2$ for clarity.

Figure 10

Figure 9. Figure 9 long description.(a) Distributions of the integral time scales, tint$t_{\textit{int}}$, for Wi$\textit{Wi}$ = 8.3, 14.5, 40.2, 63.7, 71, 76.4 (from top to bottom) calculated from the temporal autocorrelation of the radial velocity fluctuations, Cur′ (τ)$C_{u'_r}\ (\tau )$, for each point. (b) Average tint$t_{\textit{int}}$, normalised by the rotational speed of the inner cylinder, Ωi$\varOmega _i$ (left axis) and the polymer relaxation time, te$t_e$ (right axis) for Wi$\textit{Wi}$ = 8.3–76.4. The error bars denote the standard deviation between different data sets, where available.

Figure 11

Figure 10. Figure 10 long description.(a) Temporal power spectral density (PSD) of the radial velocity fluctuations for Wi$\textit{Wi}$ = 2.3–76.4, averaged through different datasets. The frequency axis is normalised with te$t_e$. The cyan and green lines at the top right of the figure illustrate decay exponents of −5/3$-5/3$ and −3$-3$, respectively. The vertical line corresponds to f=0.2/te$f=0.2/t_e$ of the filtered data presented in figure 5(c). (b) The decay exponents of the curves presented in (a) for Wi$\textit{Wi}$ = 8.3–76.4. The grey shaded areas denote the Wi$\textit{Wi}$ range where turbulence suppression becomes more pronounced. (c) Non-shifted temporal PSD of the radial velocity fluctuations. Only the cases of Wi$\textit{Wi}$ = 8.3 and Wi$\textit{Wi}$ = 76.4 are shown for clarity. The cyan and green lines at the top right of the figure illustrate decay exponents of −5/3$-5/3$ and −3$-3$, respectively.

Figure 12

Figure 11. Figure 11 long description.(a) Normalised pdfs of the radial velocity spatial differences, δur/Ωiri$\delta u_r/\varOmega _i r_i$, along the centre of the gap for the smallest spatial lag, ξz/d$\xi _z/d$ = 0.04. (b) The excess kurtosis (Kurtosis$\textit{Kurtosis}$-3) of the distributions compared with the Gaussian case for spatial lags ξz/d$\xi _z/d$ = 0–1.5. Both figures are plotted for Wi$\textit{Wi}$ = 0–76.4.

Figure 13

Figure 12. Figure 12 long description.(a) Second-order structure functions of the radial velocity differences, S2(ξ)=<[δur(ξ)]2>$S_2(\xi )=\lt [\delta u_r(\xi )]^2\gt$ for Wi$\textit{Wi}$ = 0–76.4 and ξ/d$\xi /d$ = 0–1.4 and (b) S2(ξ)$S_2(\xi )$ curves presented in (a), compensated with the gradient of the viscous dissipation regime, (ξ/d)2$(\xi /d)^2$. The square markers denote the deflection points from this scaling. All curves are shifted vertically for clarity.

Figure 14

Figure 13. Figure 13 long description.(a) The excess kurtosis (Kurtosis$\textit{Kurtosis}$-3) of the temporal differences of the radial velocities distributions compared with the Gaussian case for temporal lags τ/te$\tau /t_e$ = 0–1.5. The vertical dash-dotted line corresponds to the peaks of the curves at τ/te≈$\tau /t_e \approx$ 0.2–0.3. (b) Pdfs of the two-dimensional turbulent velocity fluctuations K$\mathcal{K}$. Both figures are plotted for the turbulent cases, Wi$\textit{Wi}$ = 8.3–76.4.

Figure 15

Figure 14. Figure 14 long description.Absolute values of Reynolds stresses in the r–z plane, τrz′=|ur′uz′|$\tau '_{rz}=| {u'_r u'_z}|$ (mm2s−2$\mathrm{mm^2 \boldsymbol{\, }s^{-2}}$), the turbulent velocity fluctuations K=(ur′)2+(uz′)2/3$\mathcal{K}=\sqrt {(u'_{r})^2+(u'_{z})^2}/3$ (mms−1$\mathrm{mm \boldsymbol{\, }s^{-1}}$) and for Wi$\textit{Wi}$ = 0–76.4. Units are omitted from the figure for clarity. The Q-criterion isosurfaces (Q⩾$Q\geqslant$ 15 s−2$\mathrm{s^{-2}}$) are also shown for every case. All values are computed in an area around the axial centre of the TC cell equal to the gap between the two cylinders.

Figure 16

Figure 15. Figure 15 long description.Temporal evolution of the globally averaged (a) absolute Reynolds stresses, τrz,G′ (mm2s−2)$\tau '_{rz,G}\ \mathrm{(mm^2 \boldsymbol{\, }s^{-2})}$, and (b) turbulent velocity fluctuations KG (mms−1)$\mathcal{K}_G\ \mathrm{(mm \boldsymbol{\, }s^{-1})}$ for the same time intervals as in figure 14 and indicative Wi$\textit{Wi}$ values. The metrics are obtained by averaging over the entire axial and radial extent of the PIV domain. Units are omitted from the figure for clarity.

Figure 17

Figure 16. Figure 16 long description.(a) Instantaneous velocity vectors with local two-dimensional turbulent velocity fluctuations, (K$\mathcal{K}$) contours superimposed for Wi$\textit{Wi}$ = 76.4. (b) The K$\mathcal{K}$ values along the axial direction of (a), averaged across the gap and filtered using a moving average equal to the gap size (D=d$D=d$). Red and blue colours highlight active and hibernating regions, respectively. (c) Indicative spatio-temporal maps of gap-averaged K$\mathcal{K}$ values for (i) Wi$\textit{Wi}$ = 40.2 and (ii) Wi$\textit{Wi}$ = 76.4, highlighting active/hibernating periods. The Q-criterion isosurfaces (Q⩾$Q\geqslant$ 15 s−2$\mathrm{s^{-2}}$) are also shown for the two cases. Panel (c) uses the same colour map as panel (a), with white colour corresponding to the critical value Kcr$K_{cr}$ = 2.

Figure 18

Figure 17. Figure 17 long description.(a) The median value of τrz′$\tau '_{rz}$ during active (τrz′>τrz,cr′$\tau '_{rz}\gt \tau '_{rz,cr}$, red line) and hibernating (τrz′<τrz,cr′$\tau '_{rz}\lt \tau '_{rz,cr}$, blue line) turbulence. (b) Average duration of active (ta$t_a$) and hibernating events (th$t_h$) for Wi$\textit{Wi}$ = 8.3–76.4. The fraction of time spent in hibernation relative to the total observation time is denoted by S$S$. (c) Flow cycle time scale, estimated based on the active/hibernating events’ average duration, Tcycle=ta+th$T_{\textit{cycle}} ={t_a+t_h}$, and the integral time scale, tint$t_{\textit{int}}$, as obtained by the autocorrelation analysis, normalised with the polymer relaxation time, te$t_e$. The results are shown for the turbulent cases, Wi$\textit{Wi}$ = 8.3–76.4. The grey shaded areas denote the Wi$\textit{Wi}$ range where hibernation becomes more pronounced, and the error bars denote the standard deviation between different data sets, where available.

Figure 19

Figure 18. Figure 18 long description.Joint probability density functions (j-pdfs) of vortex location and vorticity magnitude for the total flow, hibernating and active states ((a,b,c), respectively) for the turbulent cases, Wi$\textit{Wi}$ = 8.3–76.4. All figures are normalised with the maximum value, with yellow corresponding to 1 and blue to 0.

Figure 20

Figure 19. Figure 19 long description.(a) Non-normalised average magnitude of radial velocities at the inflow (orange line), ur,in¯$\overline {u_{r,in}}$, and outflow (blue line), ur,out¯$\overline {u_{r,out}}$ boundaries for Wi$\textit{Wi}$ = 0–76.4. (b) Non-normalised maximum root-mean-square of the radial velocity fluctuations, max(ur,rms′)$max(u'_{r,rms})$. (c) Non-normalised azimuthal vorticity magnitude |Ωθ|$|\varOmega _{\theta }|$ (left axis) and magnitude of the root-mean-square of azimuthal vorticity fluctuations, |Ωθ,rms′|$|\varOmega '_{\theta ,rms}|$ (right axis). The error bars denote the standard deviation between different data sets, where available.

Figure 21

Figure 20. Figure 20 long description.Spatio-temporal maps of the instantaneous filtered radial velocities, ur,filt$u_{r,filt}$, for Wi$\textit{Wi}$ = 0–76.4. The velocities are averaged across the gap and are shown over a period of 5 s.

Figure 22

Figure 21. Figure 21 long description.Spatio-temporal maps of azimuthal vorticity, Ωθ$\varOmega _{\theta }$, calculated from the original (a) and filtered (b) velocities for Wi$\textit{Wi}$ = 0–76.4. The vorticity is averaged across the gap and shown over a period of 5 s.

Figure 23

Figure 22. Figure 22 long description.Average duration of active (ta$t_a$) and hibernating events (th$t_h$) for Wi$\textit{Wi}$ = 8.3–76.4. The fraction of time spent in hibernation relative to the total observation time is denoted by S$S$. The results are presented for different thresholds of the two-dimensional turbulent velocity fluctuations Kcr$\mathcal{K}_{cr}$.

Figure 24

Figure 23. Figure 23 long description.Average duration of active (ta$t_a$) and hibernating events (th$t_h$) for Wi$\textit{Wi}$ = 8.3–76.4. The fraction of time spent in hibernation relative to the total observation time is denoted by S$S$. The results are presented for different moving average lengths D$D$.

Figure 25

Figure 24. Figure 24 long description.Sensitivity analysis of (a) two-dimensional turbulent velocity fluctuations Kcr$\mathcal{K}_{cr}$ and (b) moving average lengths D$D$ on the normalised flow cycle time scale, Tcycle/te$T_{\textit{cycle}}/t_e$, and the integral time scale tint/te$t_{\textit{int}}/t_e$.