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Evanescent and inertial-like waves in rigidly rotating odd viscous liquids

Published online by Cambridge University Press:  26 September 2024

E. Kirkinis*
Affiliation:
Department of Materials Science & Engineering, Robert R. McCormick School of Engineering and Applied Science, Northwestern University, Evanston, IL 60208, USA Center for Computation and Theory of Soft Materials, Northwestern University, Evanston, IL 60208, USA
M. Olvera de la Cruz
Affiliation:
Department of Materials Science & Engineering, Robert R. McCormick School of Engineering and Applied Science, Northwestern University, Evanston, IL 60208, USA Center for Computation and Theory of Soft Materials, Northwestern University, Evanston, IL 60208, USA
*
Email address for correspondence: kirkinis@northwestern.edu

Abstract

Three-dimensional non-rotating odd viscous liquids give rise to Taylor columns and support axisymmetric inertial-like waves (J. Fluid Mech., vol. 973, 2023, A30). When an odd viscous liquid is subjected to rigid-body rotation however, there arise in addition a plethora of other phenomena that need to be clarified. In this paper, we show that three-dimensional incompressible or two-dimensional compressible odd viscous liquids, rotating rigidly with angular velocity $\varOmega$, give rise to both oscillatory and evanescent inertial-like waves or a combination thereof (which we call of mixed type) that can be non-axisymmetric. By evanescent, we mean that along the radial direction, typically when moving away from a solid boundary, the velocity field decreases exponentially. These waves precess in a prograde or retrograde manner with respect to the rotating frame. The oscillatory and evanescent waves resemble respectively the body and wall-modes observed in (non-odd) rotating Rayleigh–Bénard convection (J. Fluid Mech., vol. 248, 1993, pp. 583–604). We show that the three types of waves (wall, body or mixed) can be classified with respect to pairs of planar wavenumbers $\kappa$ which are complex, real or a combination, respectively. Experimentally, by observing the precession rate of the patterns, it would be possible to determine the largely unknown values of the odd viscosity coefficients. This formulation recovers as special cases recent studies of equatorial or topological waves in two-dimensional odd viscous liquids which provided examples of the bulk–interface correspondence at frequencies $\omega <2\varOmega$. We finally point out that the two- and three-dimensional problems are formally equivalent. Their difference then lies in the way data propagate along characteristic rays in three dimensions, which we demonstrate by classifying the resulting Poincaré–Cartan equations.

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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 in any medium, provided the original work is properly cited.
Copyright
© The Author(s), 2024. Published by Cambridge University Press
Figure 0

Figure 1. Wall and body modes (or evanescent and oscillatory inertial-like waves, respectively), and mixed mode of the fields (density or pressure $\sim {\rm J}_m(\kappa r)$, where ${\rm J}_m$ is the Bessel function of the first kind and $m$ an integer determining periodicity in the azimuthal direction), for a rigidly rotating odd viscous liquid with angular velocity $\varOmega$, in two and three dimensions, satisfying no-slip boundary conditions. Each mode can be classified according to the character of the planar wavenumber $\kappa$, cf. table 1. Body modes: prominent in the interior of the cylinder. Wall modes: prominent near the side wall. Mixed modes: a combination of the previous two behaviours.

Figure 1

Table 1. Types of roots $\kappa$ displayed in figure 3, from (2.12) $\nu _o\kappa ^2 = \alpha \pm \sqrt {\alpha ^2 + \beta }$ according to the sign of the parameters $\alpha = {\omega ^2}/{2\varOmega _o} - 2\varOmega$ and $\beta = \omega ^2 - (2\varOmega )^2$ defined in (2.13a,b). The last column defines the terminology employed in this paper to describe the physical effect.

Figure 2

Figure 2. Two-dimensional odd viscous compressible liquid rotating with angular velocity $\varOmega$. In plane polar coordinates, the velocity field is ${\boldsymbol {v}} = v_r \hat {{\boldsymbol {r}}} + v_\phi \hat {\boldsymbol {\phi }}$ in the frame rotating with the liquid at constant angular velocity $\varOmega$.

Figure 3

Figure 3. Roots of (2.12) in the parameter space $(\alpha,\beta )$ defined in (2.13a,b) giving rise to the wall and body modes depicted in figure 1 according to whether $\kappa$ is real, imaginary or complex. Here, $\alpha$ and $\beta$ have units of frequency and square frequency, respectively.

Figure 4

Figure 4. Real frequency $\omega$ versus the real and imaginary parts of the eigenvalue $\kappa$ derived as a solution of (2.12). Both panels emphasize the presence of imaginary or complex values of $\kappa$ that cannot be captured by a plane-wave analysis of the momentum equations. In particular, the domain $\omega <2\varOmega$ is populated by imaginary or complex $\kappa$ that may give rise to wall (evanescent wave) modes (the character of $\kappa$ is displayed in figure 3). Note that the indicated curves are symmetric with respect to the $\omega =0$ plane and continuously extend towards negative $\omega$ values. The parameters are given in arbitrary units. (a) $(c, \varOmega, \nu _o, \rho ) = (8, -20, 0.1, 1)$. (b) $(c, \varOmega, \nu _o, \rho ) = (15, -500, 2, 1)$.

Figure 5

Figure 5. Density profiles and contours for the wall modes arising when the parameter $\kappa$ lies in the lower left of the diagram in figure 3 (two imaginary pair $\kappa$ values) and thus the frequencies lie in the ‘gap’ $(-2\varOmega, 2\varOmega )$. (a,c) $m=2$ mode, with $(\omega, \nu _o) = (0.4, 6.4)$ as solution of system (2.17) leading to $(\kappa _1, \kappa _2) = (-1.95i, -3.2i)$. (b,d) $m=5$ mode, with $(\omega, \nu _o) = (1.5, 2.5)$ as a solution of system (2.17) leading to $(\kappa _1, \kappa _2) = (-2.7i, -5.9i)$. In both cases, $(c, \varOmega, \rho _0, R) = (8, 20, 1,10)$ and thus both profiles precess in a prograde manner in the frame rotating with the liquid. Note the resemblance of the density profiles with the temperature distribution of rapidly rotating (non-odd) Rayleigh–Bénard convection in Goldstein et al. (1993, figure 6) and of the contour plots with those of Souslov et al. (2019, figures 3 and S3). Observing experimentally the precession rate of patterns could, in principle, lead to the determination of the odd viscosity coefficient. Parameter and observable units are arbitrary.

Figure 6

Figure 6. Admissible $(\nu _o, \omega )$ pairs, as a solution of system (2.17), giving rise to the wall modes displayed in figure 5 employing the latter figure's parameter values. Thus, observing experimentally the precession rate of patterns $\omega$, it would be possible, in principle, to determine the largely unknown value of the odd viscosity coefficient $\nu _o$. Arbitrary units of the parameters were employed.

Figure 7

Figure 7. A body mode for $m=5$ with $(\omega, \nu _o) = (34.6,$$-2.8)$ as a solution of system (2.17) leading to $(\kappa _1, \kappa _2) = ($$-4.2, 1.7)$, and the same parameters as in figure 5. Thus, the admissible $\kappa$ values are located in the lower right of figure 3. The patterns precess in the rotating frame in a prograde manner. Note the resemblance of the density profiles with the temperature distribution of non-odd rapidly rotating Rayleigh–Bénard convection in Goldstein et al. (1993, figure 7). Observing experimentally the precession rate of patterns could, in principle, lead to the determination of the odd viscosity coefficient. Units employed above are arbitrary.

Figure 8

Table 2. Conventions of odd viscosity coefficients that have appeared in the literature.

Figure 9

Figure 8. Three-dimensional odd viscous liquid rotating with angular velocity $\varOmega$ about the $\hat {{\boldsymbol {z}}}$ axis. In cylindrical coordinates, the velocity field is ${\boldsymbol {v}} = v_r \hat {{\boldsymbol {r}}} + v_\phi \hat {\boldsymbol {\phi }} + v_z \hat {{\boldsymbol {z}}}$ in the frame of reference rotating with the liquid.

Figure 10

Figure 9. Real frequency $\omega$ versus the real and imaginary parts of the eigenvalue $\kappa$ derived as a solution of (3.13). Both panels emphasize the presence of imaginary or complex values of $\kappa$ that cannot be captured by a plane-wave analysis of the momentum equations. In particular, the domain $\omega <2\varOmega$ is populated by imaginary or complex $\kappa$ values that exclusively give rise to wall (evanescent wave) modes. Note that the indicated curves are symmetric with respect to the $\omega =0$ plane. Units employed above are arbitrary. (a) $(\varOmega, \nu _o, k) = (5, 1, 1)$. (b) $(\varOmega, \nu _o, k) = (5, 10, 1)$.

Figure 11

Figure 10. Precessing axial velocity (or pressure) profiles and contours for the modes arising when the parameter $\kappa$ lies in the upper part (two real two imaginary) and lower right section of the diagram in figure 3 (four real $\kappa$ values), respectively. (a,c) $m=2$ mixed mode, with $(\omega, \nu _o) = (-0.9, -3.3)$ as a solution of system (2.17) leading to $(\kappa _1, \kappa _2) = (-0.97, -0.5i)$. (b,d) $m=5$ body mode, with $(\omega, \nu _o) = (0.3,-3 )$ as a solution of system (2.17) leading to $(\kappa _1, \kappa _2) = (-0.75, 0.3)$. In both cases, $(k, \varOmega, R) = (1, 1, 10)$ in arbitrary units. The odd viscosity coefficients were chosen to satisfy $\nu _o=2\nu _4$, as explained in (3.23). Observing experimentally the precession rate of patterns could, in principle, lead to the determination of the odd viscosity coefficients $\nu _o$ and $\nu _4$. Units employed above are arbitrary.

Figure 12

Figure 11. Instantaneous streamlines in the $r\unicode{x2013}z$ plane of the velocity field (3.30)–(3.32), representing a forced harmonic wave propagating in the $z$ direction according to (3.26). The liquid is confined between the forced inner cylinder at $r=R_1=2 + {\rm Re}\,\eta$ and the immobile external cylinder at $r=R_2=4$ (in arbitrary units).

Figure 13

Figure 12. Distribution of pressure (colourbar: ${\rm dyne}\ \textrm {cm}^{-2}$) in an odd viscous liquid entering into a rectangular channel from the right, moving slowly with velocity $U=0.01\ {\rm cm}\ {\rm s}^{-1}$, and meeting a centred solid immobile sphere (of radius $6$ cm). Stokes flow with $\eta _4 = 0.2\ {\rm g}\ ({\rm cm}\ {\rm s})^{-1}$ and $\eta _o = 0$ from the constitutive law (3.1), shear viscosity that of water and with no-slip boundary conditions on the channel walls. In both panels, data propagate along directions making a $45^\circ$ angle with the horizontal (along the Monge cone $z = \pm r$ in (B12)). Since the depth of the box is narrow, the data in panel (b) are reflected on its walls located at $y=\pm 20$ cm. Numerical simulations were performed with the finite-element package Comsol.

Figure 14

Figure 13. (a) Colourbar: distribution of radial component of velocity $v_r$ (${\rm cm}\ {\rm s}^{-1}$), (where the liquid velocity is denoted by ${\boldsymbol {v}} = v_r \hat {{\boldsymbol {r}}} + v_\phi \hat {\boldsymbol {\phi }} + v_z \hat {{\boldsymbol {z}}}$ in cylindrical coordinates) and (b) pressure $p$ (${\rm dyne}\ \textrm {cm}^{-2}$) in an odd viscous liquid moving slowly and meeting an immobile sphere (of radius $3.8$ cm) located at elevation $z=50$ cm at the centre axis of a cylinder. Here $\eta _4 = 2\ {\rm g}\ ({\rm cm}\ {\rm s})^{-1}$, $\eta _o = 0.1\ {\rm g} ({\rm cm}\ {\rm s})^{-1}$ from constitutive law (3.1) and shear viscosity is that of water. Liquid enters from the top ($z=100$ cm) and exits at the bottom ($z=0$) of the cylinder. The sphere is not allowed to rotate. White lines are liquid streamlines. In all cases, data emanating from the sphere propagate along rays that lie on the Monge cone $z \sim \pm r$ defined in (B12). A column circumscribing the sphere, whose generators are parallel to the $z$ axis is also present. It becomes visible in a plot of the flow structure along the full expanse of the cylinder, see figure 14. Numerical simulations were performed with the finite-element package Comsol.

Figure 15

Figure 14. Colourbar: distribution of minus the axial velocity $v_z$ (${\rm cm}\ {\rm s}^{-1}$) (the $z$ component of the liquid velocity ${\boldsymbol {v}} = v_r \hat {{\boldsymbol {r}}} + v_\phi \hat {\boldsymbol {\phi }} + v_z \hat {{\boldsymbol {z}}}$ whose strength is displayed in the colourbar) in an odd viscous liquid moving slowly and meeting an immobile sphere (of radius $3.8$ cm) located at elevation $z=50$ cm at the centre axis of a cylinder (figure 13 shows an $r$$z$ slice of this cylinder). Liquid enters from the top ($z=100$ cm) and exits at the bottom ($z=0$). The sphere is not allowed to rotate. The presence of a central Taylor column circumscribing the sphere is visible and it is attributed to the straight-line characteristics (B7) parallel to the anisotropy $z$ axis. The presence of rays making (nearly) a $45^\circ$ angle with the horizontal is also visible. They are attributed to the characteristics that lie on the Monge cone (B12). $\eta _4 = 2\ {\rm g}\ ({\rm cm}\ {\rm s})^{-1}$, $\eta _o = 0.1\ {\rm g}\ ({\rm cm}\ {\rm s})^{-1}$ from constitutive law (3.1) and shear viscosity is that of water, as in figure 13. Numerical simulations were performed with the finite-element package Comsol.

Figure 16

Figure 15. Initial data of density $\rho _0(x,y)$ in a compressible two-dimensional odd viscous liquid propagate along straight characteristic lines according to (C4a,b), forming a temporal Taylor column.

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