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Reciprocal swimming at intermediate Reynolds number

Published online by Cambridge University Press:  18 November 2022

Nicholas J. Derr*
Affiliation:
Department of Mathematics, Massachusetts Institute of Technology, Cambridge, MA 02139, USA John A. Paulson School of Engineering and Applied Sciences, Harvard University, Cambridge, MA 02138, USA
Thomas Dombrowski
Affiliation:
Department of Applied Physical Sciences, University of North Carolina at Chapel Hill, Chapel Hill, NC 27599, USA
Chris H. Rycroft
Affiliation:
Department of Mathematics, University of Wisconsin–Madison, Madison, WI 53706, USA Computational Research Division, Lawrence Berkeley Laboratory, Berkeley, CA 94720, USA
Daphne Klotsa
Affiliation:
Department of Applied Physical Sciences, University of North Carolina at Chapel Hill, Chapel Hill, NC 27599, USA
*
†Email address for correspondence: derr@mit.edu

Abstract

In Stokes flow, Purcell's scallop theorem forbids objects with time-reversible (reciprocal) swimming strokes from moving. In the presence of inertia, this restriction is eased and reciprocally deforming bodies can swim. A number of recent works have investigated dimer models that swim reciprocally at intermediate Reynolds numbers ${\textit Re} \approx 1$–1000. These show interesting results (e.g. switches of the swim direction as a function of inertia) but the results vary and seem to be case specific. Here, we introduce a general model and investigate the behaviour of an asymmetric spherical dimer of oscillating length for small-amplitude motion at intermediate ${\textit {Re}}$. In our analysis we make the important distinction between particle and fluid inertia, both of which need to be considered separately. We asymptotically expand the Navier–Stokes equations in the small-amplitude limit to obtain a system of linear partial differential equations. Using a combination of numerical (finite element) and analytical (reciprocal theorem, method of reflections) methods we solve the system to obtain the dimer's swim speed and show that there are two mechanisms that give rise to motion: boundary conditions (an effective slip velocity) and Reynolds stresses. Each mechanism is driven by two classes of sphere–sphere interactions, between one sphere's motion and (1) the oscillating background flow induced by the other's motion, and (2) a geometric asymmetry induced by the other's presence. We can thus unify and explain behaviours observed in other works. Our results show how sensitive, counterintuitive and rich motility is in the parameter space of finite inertia of particles and fluid.

Information

Type
JFM Papers
Copyright
© The Author(s), 2022. Published by Cambridge University Press
Figure 0

Figure 1. Kinematic and dynamic model schematics. (a) The model system consists of a pair of spheres, labelled $j=1$ or 2, with oscillating centre positions $\smash {z_j(t) = \bar {z}_j + \hat {z}_j \,{\rm e}^{{\rm i}\omega t}}$. The distance between the spheres is $\smash {\zeta (t) = d + \varDelta \,{\rm e}^{{\rm i}\omega t}}$, with $\smash {d = \bar {z}_2 - \bar {z}_1}$ and $\smash {\varDelta =\hat {z}_2-\hat {z}_1}$. The spheres are not generally in-phase, such that sphere 1 leads the other by a phase difference $\phi$. (b) Each sphere is subject to two applied forces. The central connector exerts a pair of equal and opposite, time-dependent forces $\smash {F_2^{(i)} = -F_1^{(i)}}$, defined to produce the kinematics in (a). The resulting motion induces fluid-mediated forces $\smash {F_j^{(f)}}$ applied via surface tractions over the sphere surfaces. These include Stokes drag, the Basset force and the added mass effect. (c) The spheres’ velocity Fourier magnitudes $\smash {\hat {U}_j}$ are plotted in the complex plane, illustrating the relationship between the phase difference $\phi$ and the individual phase lags $\phi _j$ between the spheres’ oscillation and that of the separation rate of change, which has complex Fourier amplitude $\smash {i \omega \varDelta = \hat {U}_2 - \hat {U}_1 \propto 1}$.

Figure 1

Table 1. List of symbols used in this paper.

Figure 2

Figure 2. The steady flow field as a function of fluid inertia $M^2$, plotted via streamlines in the reference frame of the swimmer. Vorticity is denoted with colour. (a) At small $M^2$ the dimer acts as a ‘puller’, attracting fluid along its axis of symmetry and ejecting it radially as it swims in the direction of the small sphere. This produces an approximately Stokesian straining flow. (b,c) For intermediate $M^2$, there exists a boundary layer outside of which the flow is noticeably weaker. As $M^2$ grows, the inner layer grows thinner. (d) At large $M^2$, the dimer swims toward the large sphere and acts as a pusher. Parameters: $(a_1,a_2,{d},\rho _1,\rho _2) = (1/2,1,3,1,1)$.

Figure 3

Figure 3. Survey of net dimer swim speeds (a–c.i) and contributions from each mechanism (a–c.ii) for three representative systems. In all cases, $\{a_1,a_2,{d}\} = \{1/2,1,3\}$. (a) For equal-density spheres and fluid $\rho _1=\rho _2 = 1$, the dimer undergoes a switch in direction when the contribution from the Reynolds stress ($\bar {U}_r$), driving motion towards the large sphere, overcomes that of the boundary velocity ($\bar {U}_b$), which favours motion towards the small sphere. In (a.i) the blue dots correspond to the flow fields presented in figure 2. (b) If $m_1 > m_2$ the dimer may experience two direction switches as shown here, and the mechanism-specific swim speeds $\bar {U}_b$ and $\bar {U}_r$ are not monotonic. (c) In Stokes flow ($M^2 = 0$) with $\rho _1 = \rho _2$, there is no change in swimming direction, and no motion at large $S^2$.

Figure 4

Figure 4. Swim speeds as a function of solid inertia for varying fluid–solid inertia ratios. The $M^2 = 0$ case is plotted as a black dashed line, and $\rho _1 = \rho _2$ for all cases. (a) Contributions to the swim speed from the boundary velocity $(\bar {U}_b)$ and Reynolds stress $(\bar {U}_r)$ are plotted as a function of the solid inertia $S^2$ for a variety of $M^2/S^2$. Note that $\bar {U}_r = 0$ for $M^2 = 0$. (b) The dimer swim speed is plotted for the same fluid–solid inertia ratios. Parameters: $\{a_1,a_2,{d}\} = \{1/2,1,3\}$.

Figure 5

Figure 5. Schematic of the method of reflections for calculating the Brinkman flow field around two spheres undergoing axisymmetric relative motion. A set of coefficients $c^{(-k,0)}$ represents the exact solution of the flow about sphere $k$ in unbounded fluid, but the presence of this flow violates the boundary conditions at the other sphere $m$. This incident flow can be described in terms of harmonics about sphere $m$ by a set of coefficients $c^{(+m,1)}$, and the spheres’ resistance to deformation creates a reflection flow $c^{(-m,1)}$ that exactly cancels out the incident flow at sphere $m$. However, this induces a new incident flow at sphere $k$ described by $c^{(+k,2)}$. This process can be repeated and truncated after a specified number of iterations. Each set of coefficients are linearly related to those they are induced by. Here, all the red coefficients are proportional to $\hat {U}_2$, and all the blue to $\hat {U}_1$.

Figure 6

Figure 6. Schematic of the types of sphere interactions and their relation to products of the complex Fourier amplitudes $\smash {\hat {U}_1}$ and $\smash {\hat {U}_2}$. Sphere interactions can be decomposed into geometric and flow contributions. The presence of the other sphere creates a time-invariant geometric asymmetry akin to an oscillating sphere near a wall (a). Each sphere is also moving within an oscillating background flow generated by the motion of the other (b). By linearity, we can associate products of the velocity amplitudes $\smash {\hat {U}_j \hat {U}_k^*}$ with the different interaction types. The geometric interactions correspond to products of each sphere's amplitude with itself, and the flow interactions to the product of both spheres’ amplitudes.

Figure 7

Table 2. Leading-order scalings of the velocity amplitude magnitudes $|\hat {U}_k|$ and trigonometric functions of the sphere phase difference $\phi$. The second and third columns correspond to the small- and large-inertia limits in the presence of non-zero fluid inertia $(M^2 \ne 0)$, and the fourth and fifth columns are the same limits for Stokes flow $(M^2 = 0)$. For the $M^2 \ne 0$ case, values are given in terms of the effective mass $m_k$(3.9). For Stokes flow, rescalings of the actual sphere masses $\tilde {m}_k$(4.15) are used.

Figure 8

Figure 7. Normalised swim speeds at low fluid inertia for an equal-density swimmer with $\rho _1 = \rho _2 = 1$. The swim speed contributions from the boundary velocity $\smash {\bar {U}_b}$ (d–f) and Reynolds stress $\smash {\bar {U}_r}$ (a–c) are plotted with respect to $M^2 \le 1$ for a variety of small sphere radii $a_1$ (denoted by line colour) and separation distances $d$ (separated by column.) In each plot, a black vertical line marks where $M d = 1$. For points to the left of this line, the spheres lie within the others’ Brinkman boundary layer. To the right of the line, the boundary layers are small and do not extend to the other sphere. The speeds are scaled by $\smash {C^{(b/r)}_{-}}$, given by (4.21a,b) and (4.23a,b), and lie parallel to the dashed line of slope 1, showing that in this region $\smash {\bar {U}_{b/r} \approx C^{(b)}_- M^2}$ within the boundary layers.

Figure 9

Figure 8. Normalised swim speeds at high fluid inertia for an equal-density swimmer with $\rho _1 = \rho _2 = 1$. The swim speed contributions from the boundary velocity $\smash {\bar {U}_b}$ (d–f) and Reynolds stress $\smash {\bar {U}_r}$ (a–c) are plotted with respect to $M^2 \ge 1$ for a variety of small sphere radii $a_1$ (denoted by line colour) and separation distances $d$ (separated by column.) The speeds are scaled by the large-$M^2$ coefficient $\smash {C_+}$ from (4.25a,b) and (4.27). The lines’ approaching the 1/2 slope of the dashed line indicate that at high levels of inertia $\bar {U}_{b/r} \approx C_+M$. There is little variation with respect to $d$, as the spheres exist outside of each others’ boundary layers for all of the provided inertial range.

Figure 10

Figure 9. Plots of the total swim speed $\bar {U}$ as a function of fluid inertia $M^2$. (a) The swim speed is plotted for a system with $a_1 = 1/2$ and $d = 3$ for a variety of effective mass ratios $m_1/m_2$. Positive values correspond to motion towards sphere 2. At high $M^2$, motion is towards the more massive sphere. (b) The normalised swim speed $\smash {\bar {U} / \bar {U}_\infty }$ is plotted over the same range of inertia. Positive values here correspond to motion in the same direction as the theoretical limiting value $\bar {U}_\infty$(4.29) as $M^2 \to \infty$. The collapse indicates consistent scaling across mass ratios.