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Fluctuating hydrodynamics of an autophoretic particle near a permeable interface

Published online by Cambridge University Press:  31 October 2024

Günther Turk*
Affiliation:
Princeton Materials Institute, Princeton University, Princeton, NJ 08544, USA
Ronojoy Adhikari
Affiliation:
DAMTP, Centre for Mathematical Sciences, University of Cambridge, Wilberforce Road, Cambridge CB3 0WA, UK The Institute of Mathematical Sciences-HBNI, CIT Campus, Chennai 600113, India
Rajesh Singh
Affiliation:
Department of Physics, IIT Madras, Chennai 600036, India
*
†Email address for correspondence: guenther.turk@princeton.edu

Abstract

We study the autophoretic motion of a spherical active particle interacting chemically and hydrodynamically with its fluctuating environment in the limit of rapid diffusion and slow viscous flow. Then, the chemical and hydrodynamic fields can be expressed in terms of integrals. The resulting boundary-domain integral equations provide a direct way of obtaining the traction on the particle, requiring the solution of linear integral equations. An exact solution for the chemical and hydrodynamic problems is obtained for a particle in an unbounded domain. For motion near boundaries, we provide corrections to the unbounded solutions in terms of chemical and hydrodynamic Green's functions, preserving the dissipative nature of autophoresis in a viscous fluid for all physical configurations. Using this, we give the fully stochastic update equations for the Brownian trajectory of an autophoretic particle in a complex environment. First, we analyse the Brownian dynamics of particles capable of complex motion in the bulk. We then introduce a chemically permeable planar surface of two immiscible liquids in the vicinity of the particle and provide explicit solutions to the chemo-hydrodynamics of this system. Finally, we study the case of an isotropically phoretic particle hovering above an interface as a function of interfacial solute permeability and viscosity contrast.

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JFM Papers
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Copyright
© The Author(s), 2024. Published by Cambridge University Press.
Figure 0

Table 1. Governing differential laws. This table summarises the chemo-hydrodynamic coupling at the surface of an autophoretic particle, an example of two three-dimensional partial differential equations, namely the Laplace equation for the concentration field (Ia) and the Stokes equation for the fluid flow and pressure in a fluid with thermal force density $\boldsymbol {\xi }$ (Id), coupling on a two-dimensional surface only (Melcher & Taylor 1969). The chemo-hydrodynamic coupling (Ig) leads to the specified active flux $j^{\mathcal {A}}$ driving a slip flow $\boldsymbol {v}^{\mathcal {A}}$ in a thin layer at the surface of the particle with specified phoretic mobility $\mu _{c}$, finally driving the fluid surrounding the particle and causing self-propulsion. A passive particle is a rigid sphere of radius $b$ with the boundary condition: $\boldsymbol {v}^{\mathcal {D}}(\boldsymbol {b})=\boldsymbol {V}+\boldsymbol {\varOmega }\times \boldsymbol {b}$, where $\boldsymbol {V}$ is the velocity and $\boldsymbol {\varOmega }$ is the angular velocity of the particle. An active particle is modelled as a sphere with boundary condition (If), which comprises both slip $\boldsymbol {v}^{\mathcal {A}}(\boldsymbol {b})$ and rigid-body motion $\boldsymbol {v}^{\mathcal {D}}(\boldsymbol {b})$ (Anderson 1989; Ebbens & Howse 2010).

Figure 1

Table 2. Governing integral laws. This table summarises the formal solutions to the boundary-domain integral equations corresponding to the Laplace equation for the concentration $c$ (IIa) and the Stokes equation for the traction (force per unit area) $\boldsymbol {f}$ (IIf) on the surface of the particle. Here, $\boldsymbol {r},\tilde {\boldsymbol {r}}\in S$, where $\boldsymbol {r}=\boldsymbol {R}+\boldsymbol {b}$ and $\tilde {\boldsymbol {r}}=\boldsymbol {R}+\boldsymbol {b}'$ are the field and source points at the surface $S$ of the particle centred at $\boldsymbol {R}$, respectively, and $\int \mathrm {d}S'$ implies an integration over $\tilde {\boldsymbol {r}}$. In (IId) and (IIj) we give the solutions for the concentration and the traction in terms of integral linear operators. We have used the fact that rigid-body motion $\boldsymbol {v}^{\mathcal {D}}$ lies in the eigenspectrum of the double-layer operator (IIh) with an eigenvalue $-1/2$ (Kim 2015). In the formal solutions we have introduced operators representing the linear response to a background concentration field $\zeta$, the so-called elastance $\mathcal {E}$, the rigid-body friction $\boldsymbol {\gamma }$ and the friction due to surface slip $\hat {\boldsymbol {\gamma }}$. Inserting the operator solution for the concentration in (IIe) into (Ig) in table 1 for the chemo-hydrodynamic coupling at the surface of an autophoretic particle, we find (IIl) for the surface slip $\boldsymbol {v}^{\mathcal {A}}(\boldsymbol {b})$.

Figure 2

Figure 1. Mean-squared displacement of the programmed Brownian motion of an autophoretic particle. In panels (a–c) we compare the non-dimensionalised MSDs of translational, circular and helical swimming computed for Brownian simulations with their theoretical predictions (see the main text for the latter) at various temperatures characterised by a particle Péclet number ${Pe}$. We define ${Pe}=\infty$ (no noise), ${Pe}=100$ (moderate noise) and ${Pe}=10$ (strong noise) following Mozaffari et al. (2018). For all three types of motion a diffusive regime ${\sim }t$ can be identified above a certain persistence time broadly determined by the amount of rotational diffusivity. The insets show the respective trajectories over an arbitrary time $T$ in the limit of zero temperature.

Figure 3

Figure 2. Half-coated phoretic particle near the surface of two immiscible liquids. Schematic representation of a half-coated phoretic particle (Janus particle) of radius $b$ and with orientation $\boldsymbol {e}_{1}$ at a height $h$ above an interface of viscosity ratio $\lambda ^{f}=\eta _{2}/\eta _{1}$ and diffusivity ratio $\lambda ^{c}=D_{2}/D_{1}$. The latter effectively measures how permeable the interface is to the solutes, where $\lambda ^{c}=0$ implies an impermeable and $\lambda ^{c}=1$ a perfectly permeable interface. Due to the cylindrical symmetry of the system we can restrict our attention to the $x$–$z$ plane, where the symbols $\parallel$ and $\perp$ imply motion parallel and perpendicular to the interface, respectively.

Figure 4

Table 3. Green's functions for a plane interface. The Green's functions for the concentration (Laplace equation, left) and velocity (Stokes equation, right) fields near a plane, chemically permeable fluid–fluid interface of solute diffusivity ratio $\lambda ^{c}=D_{2}/D_{1}$ and viscosity ratio $\lambda ^{f}=\eta _{2}/\eta _{1}$ at $z=0$ are given. The particle is in the positive half-space $z>0$, where the solute diffusivity is $D_{1}$ and the fluid viscosity is $\eta _{1}$. We use $\boldsymbol {r}=\boldsymbol {R}-\tilde {\boldsymbol {R}}$ and $\boldsymbol {r}^{*}=\boldsymbol {R}-\tilde {\boldsymbol {R}}^{*}$, with the field point $\boldsymbol {R}=(x,y,z)^{\textrm {tr}}$ , the source point $\tilde {\boldsymbol {R}}=(\tilde {x},\tilde {y},\tilde {z})^{\textrm {tr}}$ and the relation $\tilde {\boldsymbol {R}}^{*}=\boldsymbol {\mathcal {M}}\boldsymbol {\cdot }\tilde {\boldsymbol {R}}$ between the physical position vector $\tilde {\boldsymbol {R}}$ and the position vector of the image singularities $\tilde {\boldsymbol {R}}^{*}$. The height of the centre of the particle above the interface is $\tilde {z}=h$. With this, we have $\tilde {\boldsymbol {R}}-\tilde {\boldsymbol {R}}^{*}=(0,0,2h)^{\textrm {tr}}.$ We define $\boldsymbol {\nabla }^{*}=\boldsymbol {\nabla }_{\boldsymbol {r}^{*}}$, $\mathcal {M}_{\beta \gamma }^{f}=(({1-\lambda ^{f}})/({1+\lambda ^{f}}))\delta _{\beta \rho }\delta _{\rho \gamma }-\delta _{\beta z}\delta _{z\gamma }$, the mirroring operator $\mathcal {M}_{\beta \gamma }=\delta _{\beta \rho }\delta _{\rho \gamma }-\delta _{\beta z}\delta _{z\gamma }$ and the index $\rho =x,y$ in the plane of the interface.

Figure 5

Table 4. Chemical coefficients. Scalar coefficients for the linear response to a background concentration field and for the elastance tensors with $\varLambda ^{c}=(1-\lambda ^{c})/(1+\lambda ^{c})$, where $\lambda ^{c}=D_{2}/D_{1}$, and the height above the interface $\hat {h}=h/b$. We have used the exact unbounded coefficients in (3.6a,b) such that $\zeta _{1}=3/2$, $\mathcal {E}_{1}=3/8{\rm \pi} bD_{1}$ and $\mathcal {E}_{2}=5/2{\rm \pi} bD_{1}$. Cylindrical symmetry of the system implies, for the coupling to a linear background concentration field, $\boldsymbol {\zeta }^{(1,1)}=(\boldsymbol {I}-\hat {\boldsymbol {z}}\hat {\boldsymbol {z}})\,\zeta _{\parallel }^{(1,1)}+\hat {\boldsymbol {z}}\hat {\boldsymbol {z}}\, \zeta _{\perp }^{(1,1)}$. The relevant elastance tensors are $\boldsymbol {\mathcal {E}}^{(1,0)}=\hat {\boldsymbol {z}}\,\mathcal {E}^{(1,0)},$ $\boldsymbol {\mathcal {E}}^{(1,1)}=(\boldsymbol {I}-\hat {\boldsymbol {z}}\hat {\boldsymbol {z}})\, \mathcal {E}_{\parallel }^{(1,1)}+\hat {\boldsymbol {z}}\hat {\boldsymbol {z}}\,\mathcal {E}_{\perp }^{(1,1)},$ $\boldsymbol {\mathcal {E}}^{(2,0)}=-(3\hat {\boldsymbol {z}}\hat {\boldsymbol {z}}-\boldsymbol {I})\,\mathcal {E}^{(2,0)}$ and $\mathcal {E}_{\alpha \beta \gamma }^{(2,1)}=\mathcal {E}^{(2,1)}[(\delta _{\gamma \alpha }-\delta _{\gamma z}\delta _{\alpha z})\delta _{\beta z}+(\delta _{\gamma \beta }-\delta _{\gamma z}\delta _{\beta z})\delta _{\alpha z}+(3\delta _{\beta z}\delta _{\alpha z}-\delta _{\alpha \beta })\delta _{\gamma z}]$.

Figure 6

Table 5. Hydrodynamic coefficients. Scalar coefficients for the mobility matrices and the relevant propulsion tensors with $\lambda ^{f}=\eta _{2}/\eta _{1}$ and the height above the interface $\hat {h}=h/b$. Cylindrical symmetry of the system allows us to write, for the translational mobilities, $\boldsymbol {\mu }^{TT}\!=(\boldsymbol {I}-\hat {\boldsymbol {z}}\hat {\boldsymbol {z}})\mu _{\parallel }^{TT}+ \hat {\boldsymbol {z}}\hat {\boldsymbol {z}}\mu _{\perp }^{TT}$ and $\boldsymbol {\mu }^{TR}\!=(\boldsymbol {\mu }^{RT})^{\textrm {tr}}\!=\mu ^{TR}\boldsymbol {\epsilon }\boldsymbol {\cdot }\hat {\boldsymbol {z}}$. The mobility $\boldsymbol {\mu }^{RR}$ has the same structure as $\boldsymbol {\mu }^{TT}$ with the corresponding coefficients $\mu _{\parallel }^{RR}$ and $\mu _{\perp }^{RR}$. The propulsion tensor for the leading symmetric slip mode is ${{\rm \pi} _{\alpha \beta \gamma }^{(T,2s)}}={\rm \pi} _{1}^{(T,2s)}[(\delta _{\gamma \alpha }-\delta _{\gamma z}\delta _{\alpha z})\delta _{\beta z}+(\delta _{\beta \alpha }-\delta _{\beta z}\delta _{\alpha z})\delta _{\gamma z}]+{\rm \pi} _{2}^{(T,2s)}(\delta _{\gamma \beta }-3\delta _{\gamma z}\delta _{\beta z})\delta _{\alpha z}$. The propulsion tensor $\boldsymbol {{\rm \pi} }^{(T,4t)}$ is of the same structure as $\boldsymbol {{\rm \pi} }^{(T,2s)}$ with the corresponding coefficients ${\rm \pi} _{1}^{(T,4t)}$ and ${\rm \pi} _{2}^{(T,4t)}$. Since $\boldsymbol {{\rm \pi} }^{(T,3t)}$ has the same structure as $\boldsymbol {\mu }^{TT}$, we adopt an analogous notation with ${\rm \pi} _{\parallel }^{(T,3t)}$ and ${\rm \pi} _{\perp }^{(T,3t)}$. For the propulsion tensors contributing to the particle's rotational dynamics we obtain ${\rm \pi} _{\alpha \beta \gamma }^{(R,2s)}={\rm \pi} ^{(R,2s)}(\delta _{\beta z}\epsilon _{z\gamma \alpha }+\delta _{\gamma z}\epsilon _{z\beta \alpha })$ and $\boldsymbol {{\rm \pi} }^{(R,3t)}={\rm \pi} ^{(R,3t)}\boldsymbol {\epsilon }\boldsymbol {\cdot }\hat {\boldsymbol {z}}$. The propulsion tensor $\boldsymbol {{\rm \pi} }^{(R,4t)}$ is of the same structure as $\boldsymbol {{\rm \pi} }^{(R,2s)}$ with the corresponding coefficient ${\rm \pi} ^{(R,4t)}$.

Figure 7

Figure 3. Chemo-hydrodynamic effects of a boundary. We compare typical trajectories of a bottom-heavy non-axisymmetric active particle (see the main text for the chosen particle specifications) near two types of chemically impermeable ($\lambda ^{c}=0$) liquid–liquid interfaces. In panels (a,b) the interface is chosen to be a free air–water surface ($\lambda ^{f}=0$) and a water–oil interface ($\lambda ^{f}\approx 50$), respectively. The temperature in these panels is zero and the starting point (orientation) of the particle is indicated by a grey disk (line). In the upper panels we compare the trajectories of the particle obtained to various orders in the inverse distance to the wall $h^{-1}$, thus gradually including more interactions with the wall. Here, ‘simulation’ refers to the full dynamical system at the accuracy obtained in this paper. The lower panels show the orientational evolution of the particle in the various approximations in a polar plot, parametrised by the angle $\vartheta$ and the distance to the starting point. There are two main features to be observed when comparing (a,b). First, the particle tends to stay further away from the water–oil interface when compared with the air–water surface. This is expected as the particle's mobility perpendicular to the interface will be reduced with increasing viscosity ratio, see table 5. Second, the approximations are better for higher viscosity ratios. Again, this can be understood intuitively when considering the example that fluid flows produced near a wall decay faster in the far field when compared with fluid flows produced near a free surface (Aderogba & Blake 1978). The slower decay of the latter means that, to achieve the same quality of approximation as with interfaces of higher viscosity ratios, higher orders in $h^{-1}$ are necessary. Panel (c) shows the same system as in panel (b) but with a finite particle Péclet number of ${Pe}=100$, representing experimentally relevant noise levels. It is clear that the translational as well as the rotational diffusion is affected by the presence of the interface. Thermal diffusion also induces a net repulsive effect between the particle and the interface.

Figure 8

Figure 4. Hovering above an interface. We show the hovering height $h$ (pseudo-colour map) for an active particle at zero temperature as a function of its activity $\mathcal {A}_{G}$ and the diffusivity ratio $\lambda ^{c}$ or the viscosity ratio $\lambda ^{f}$ of the interface. In panel (a) we consider the particle hovering above a wall ($\lambda ^{f}\rightarrow \infty$) that is permeable to the solutes. For a boundary between regions of equal solute diffusivity ($\lambda ^{c}=1$) there exists no chemical repulsion, leading to the particle inevitably crashing into the boundary. Therefore, we only consider values $\lambda ^{c} \, \leq 0.99$. The red line shows the particle's minimum activity to hover at a minimum height of $h_{{min}}=1.3$ as a function of the diffusivity ratio. The white region below the red line indicates physics that is not accessible in our simplified model and we assume that the particle crashes into the boundary due to gravity, i.e. we set $h=1$. The two dashed grey lines indicate the limiting values $\mathcal {A}_{G}^{1}\approx 500$ and $\mathcal {A}_{G}^{2}\approx 10^{5}$ that are required to hover above an impermeable and a highly permeable wall. In panel (b) we consider the particle hovering above an impermeable ($\lambda ^{c}=0$) interface of varying viscosity ratio. The two horizontal dashed grey lines indicate the limiting values $\mathcal {A}_{G}^{3}\approx 3$ and $\mathcal {A}_{G}^{1}$ that are required to hover above a free surface and a solid wall, respectively.

Figure 9

Figure 5. Solute concentration for a particle hovering above a permeable boundary. The chemical field generated by a hovering source particle (green) is shown above ($z>0$) and below ($z<0$) the permeable ($\lambda ^{c}=0.3$) boundary as a pseudo-colour map, where contours indicate regions of constant concentration. We emphasise that the net concentration (right panel) in the region containing the particle is a superposition of the source without the boundary present (a) and its image below the boundary (b). The net concentration below the permeable boundary is then generated by the appropriate boundary conditions. To imply a change in the chemical diffusivity $D_{2}=\lambda ^{c}D_{1}$ the colour map for the region $z<0$ is shown with slightly reduced opacity. Since source particles want to move down chemical gradients (anti-chemotaxis), it is clear that the image creates a repulsive concentration field in $z>0$, making it possible for the particle to hover above the boundary. It is worth noting that, for an impermeable boundary ($\lambda ^{c}=0$), the contour lines meet the boundary at a right angle and the corresponding vector field ($\boldsymbol {\nabla }c$) becomes purely tangential to this ‘no-flux’ boundary. In the limit of rapid solute diffusion the viscosity ratio of the interface has no influence on the chemical field.

Figure 10

Figure 6. Fluid flow for a particle hovering above a fluid–fluid interface. The fluid flow (laboratory frame) generated by a hovering source particle (green) is shown above ($z>0$) and below ($z<0$) a chemically permeable fluid–fluid interface ($\lambda ^{c}=0.3, \lambda ^{f}=10$). The direction of the fluid flow is indicated by black arrows, while its relative magnitude is implied by the overlaid pseudo-colour map. The net flow (c) in the region containing the particle is a superposition of the source without the boundary conditions on the fluid flow and stress (a) and its image below the boundary (b). Note that for the source the chemical boundary conditions must still be satisfied (see the net chemical field in figure 5), inducing a non-trivial slip on the otherwise isotropic particle. The net flow below the interface is then driven by the appropriate velocity and stress boundary conditions. To imply a change in the viscosity $\eta _{2}=\lambda ^{f}\eta _{1}$ the colour map for the region $z<0$ is shown with slightly reduced opacity. It is clear that the image produces an upwards flow in $z>0$ which balances gravity and makes the particle hover away from the interface. In the net flow this creates convection rolls between the particle and the interface which in turn drive convection rolls below the interface.

Figure 11

Table 6. Coefficients $c^{\alpha }$ and $q^{\beta }$ in the mobility and propulsion tensors.

Figure 12

Table 7. Big O notation for errors in the linear response to elastance, mobility and propulsion tensors.