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Slender phoretic theory of chemically active filaments

Published online by Cambridge University Press:  09 July 2020

Panayiota Katsamba
Affiliation:
School of Mathematics, University of Birmingham, Edgbaston, Birmingham B15 2TT, UK
Sébastien Michelin
Affiliation:
LadHyX – Département de Mécanique, CNRS – Ecole Polytechnique, Institut Polytechnique de Paris, 91128Palaiseau, France
Thomas D. Montenegro-Johnson*
Affiliation:
School of Mathematics, University of Birmingham, Edgbaston, Birmingham B15 2TT, UK
*
†Email address for correspondence: t.d.johnson@bham.ac.uk

Abstract

Artificial microswimmers, or ‘microbots’, have the potential to revolutionise non-invasive medicine and microfluidics. Microbots that are powered by self-phoretic mechanisms, such as Janus particles, often harness a solute fuel in their environment. Traditionally, self-phoretic particles are point like, but slender phoretic rods have become an increasingly prevalent design. While there has been substantial interest in creating efficient asymptotic theories for slender phoretic rods, hitherto such theories have been restricted to straight rods with axisymmetric patterning. However, modern manufacturing methods will soon allow fabrication of slender phoretic filaments with complex three-dimensional shapes. In this paper, we develop a slender body theory for the solute of self-diffusiophoretic filaments of arbitrary three-dimensional shape and patterning. We demonstrate analytically that, unlike other slender body theories, first-order azimuthal variations arising from curvature and confinement can make a leading-order contribution to the swimming kinematics.

Information

Type
JFM Papers
Copyright
© The Author(s), 2020. Published by Cambridge University Press
Figure 0

Figure 1.A schematic of a slender phoretic filament in three dimensions, in the shape of a helix. Surface lines are used to emphasise curvature and torsion. Laplace’s equation is solved in the bulk, with flux boundary condition on the surface of the filament $S$ determined by its activity ${\mathcal{A}}(\boldsymbol{x})|_{S}$. In later examples, we consider axisymmetric activity in the form of catalytic end caps (demarcated here by the red) with an inert midpiece, so that ${\mathcal{A}}(s)=-1$, $|s|>s_{c}$, ${\mathcal{A}}(s)=0$ otherwise.

Figure 1

Table 1.An indication of the computational savings that can be made by employing SPT over the boundary element method. Simulations run on a Macbook Pro 2.9 GHz Intel Core i7 (2017) with 16 GB 2133 MHz LPDDR3 RAM.

Figure 2

Figure 2.Summary of the different activity patterns (uniform ${\mathcal{A}}(s)=-1$, smooth decay ${\mathcal{A}}(s)=s^{2}-1$, Saturn – 2 symmetric active caps, Janus – 1 active cap), cross-sectional radius profiles (uniform, hemispherical cap used for BEM, prolate spheroid) and centreline geometries (straight, circular arc, S-shape, helix), used throughout the results section.

Figure 3

Figure 3.Validation of SPT versus the series solution of Michelin & Lauga (2017). (a) The root mean square percentage error in the surface concentration of a uniformly active prolate spheroid as calculated by SPT, as a function of the slenderness parameter $\unicode[STIX]{x1D716}$. (b) The surface concentration as a function of arclength $s$ of a set of ‘Janus’ prolate spheroids with $\unicode[STIX]{x1D716}=0.01$, with active caps such that $s_{c}<-0.9,-0.6,\ldots ,0.9$ from dark to light respectively. The solution of Michelin and Lauga is given in each case by the dashed black line. (c) Comparison of the swimming velocities of Janus prolate spheroids with $\unicode[STIX]{x1D716}=0.01$ as a function of $s_{c}$ ($-1$ all inert, 1 all active).

Figure 4

Figure 4.Validation of the first-order concentration correction $c_{1}$ of SPT versus boundary element simulation using a regularised singularity approach (Montenegro-Johnson et al.2015) with ${\mathcal{A}}(s)=s^{2}-1$ for (a) a U-shaped filament with $\unicode[STIX]{x1D6FC}=\unicode[STIX]{x03C0}/2$ and (b) an S-shaped filament with $\unicode[STIX]{x1D6FC}=\unicode[STIX]{x03C0}/3$, showing good agreement.

Figure 5

Figure 5.Validating concentration gradients against boundary element simulation, for a semicircular rod of constant radius (required for BEM). (a) For uniform activity, the slip velocity along $\unicode[STIX]{x1D703}=\unicode[STIX]{x03C0}/2$ diverges at the ends when calculated via SPT, due to the logarithmic term. (b) This divergence may be regularised by ensuring the activity smoothly decays to zero at either end. (c) Azimuthal slip flows show good agreement between SPT and BEM.

Figure 6

Figure 6.Validation of the swimming kinematics of a series of circular arcs and S-shapes as a function of the angle parameter $\unicode[STIX]{x1D6FC}$, with ${\mathcal{A}}(s)=s^{2}-1$ showing good agreement between SPT and BEM. Results obtained using the full slip flows (azimuthal and longitudinal, solid) are compared to those obtained when neglecting azimuthal slip flow ($A_{s}=A_{c}=0$ in (2.60), dashed).

Figure 7

Figure 7.The surface concentration of uniformly active phoretic filaments with a prolate spheroidal end shape and planar centrelines with (a) straight shape which is stationary but pumps fluid, (b) circular arc shape which translates and (c) S-shape which rotates. Small azimuthal variation due to non-local interactions and confinement effects from curvature are visible in the circular arc and S-shaped examples.

Figure 8

Figure 8.Leading-order contribution of azimuthal effects to kinematics arising from curvature and confinement. Kinematics of (a) circular arc and (b) S-shaped filaments versus the angle parameter based on SPT, for uniform and Saturn activity patterns, where the Saturn particle has two active end caps and an inert midpiece (see figure 2). Here, $\unicode[STIX]{x1D716}=0.01$. Solid lines include azimuthal slip flows, dashed lines have this contribution removed, i.e. $A_{s}=A_{c}=0$ in (2.60).

Figure 9

Figure 9.Qualitative schematic: understanding end shape and azimuthal effects. Red text indicates the relative concentration of solute in each figure, with slip flow (blue) moving from higher to lower concentrations, assuming constant, negative mobility. (a) The shape of the filaments affects the geometric confinement at the ends, resulting in different strength of slip flows. (b) A uniformly active prolate spheroid. For our parameter choices, azimuthal flows work in opposition to axial flows and hence the swimming direction is sensitive to which effect is stronger, which in turn depends on geometry and end shape. (c) In a capped filament azimuthal flows and axial flows work together, however, there is an opposing end-effect flow (as with the Janus prolate spheroid) that slows the swimmer.

Figure 10

Figure 10.The surface concentration of (a) a uniformly active helix and (b) a Janus helix, as calculated with SPT, with $\unicode[STIX]{x1D716}=0.01$, $\unicode[STIX]{x1D6FC}=\unicode[STIX]{x03C0}/3$, $s_{c}=-0.8$ and 2.5 turns.

Figure 11

Figure 11.Schematic showing a Janus helix, on a helical trajectory of radius $R_{T}$, from a side and top view, demonstrating the ‘exploratory area’ of the swimmer $\unicode[STIX]{x03C0}R_{T}^{2}$.

Figure 12

Figure 12.Trajectories of helical filaments with one catalytic end of length 0.1, i.e. $s_{c}=-0.9$, helical angle $\unicode[STIX]{x03C0}/3$ and varying number of turns. (a) The different helical trajectories arising from varying the number of turns. All simulations run over the same time interval ($t=30$ in dimensionless units). The axis of the trajectories is aligned with the $\unicode[STIX]{x1D734}$ vector in real space. The trajectories have been rotated to be aligned vertically for the purposes of this plot. (b) Area of helical trajectories, i.e. $\unicode[STIX]{x03C0}R_{T}^{2}$ for helical radius $R_{T}$, versus number of turns of the Janus helix. (c) Velocity along the axis of each helical trajectory versus number of turns of the Janus helix.