Alina
Arslanova
a,
Ine
Matthé
a,
Olivier
Deschaume
b,
Carmen
Bartic
b,
Wouter
Monnens
c,
Erwin Konrad
Reichel
d,
Naveen
Reddy
ef,
Jan
Fransaer
c and
Christian
Clasen
*a
aDepartment of Chemical Engineering, KU Leuven, 3001 Leuven, Belgium. E-mail: christian.clasen@kuleuven.be; Tel: +32 16 32 23 54
bDepartment of Physics, KU Leuven, 3001 Leuven, Belgium
cDepartment of Materials Engineering, KU Leuven, 3001 Leuven, Belgium
dInstitute for Microelectronics and Microsensors, Johannes Kepler University, Altenberger Strasse 69, 4040 Linz, Austria
eFaculty of Engineering Technology, University of Hasselt, Martelarenlaan 42, 3500 Hasselt, Belgium
fIMO-IMOMEC, Wetenschapspark 1, 3590 Diepenbeek, Belgium
First published on 10th August 2023
The motion of self-propelling microswimmers is significantly affected by confinement, which can enhance or reduce their mobility and also steer the direction of their propulsion. While their interactions with solid boundaries have already received considerable attention, many aspects of the influence of liquid–liquid interfaces (LLI) on active particle propulsion still remain unexplored. In this work, we studied the adsorption and motion of bimetallic Janus sideways propelled rods dispersed at the interface between an aqueous solution of hydrogen peroxide and oil. The wetting properties of the bimetallic rods result in a wide distribution of their velocities at the LLI. While a fraction of rods remain immotile, we note a significant enhancement of motility for the rest of the particles with velocities of up to 8 times higher in comparison to those observed near a solid wall. Liquid–liquid interfaces, therefore, can provide a new way to regulate the propulsion of bimetallic particles.
Confinement has a large influence on the propulsion of Janus particles and can be used to drive their motion12–14 as well as to modify their hydrodynamics15,16 and the distribution of chemical species.16,17 Propulsion near a bottom solid wall has received the most attention so far, since many chemically propelled Janus particles have metallic surfaces and thus sediment in aqueous solutions.9 Compared to the motion near a solid boundary, the propulsion near and at liquid–fluid interfaces is less studied, especially for catalytic Janus particles moving due to the chemical decomposition of a fuel. For example, an interface-induced phoresis,18,19 which involves a motion of a particle due to a symmetry breaking of the concentration of reagents or products at an interface, was predicted but never proven experimentally.
Liquid–fluid interfaces also allow the Janus particles to be irreversibly trapped and confine their motion in 2D. The number of studies on the adsorption and propulsion of active particles at liquid–fluid interfaces has significantly increased in recent years.20,21 However, the current literature on the adsorption of Janus particles at liquid–fluid interfaces is, to a great extent, focused on polar/apolar Janus particles,22,23 including studies of the influence of different shapes on their equilibrium orientation.24–27 When Janus particles have two surfaces with a large contrast in wettability, each surface tends to stay in the phase with which it has the most affinity. A typical example is a Janus Pt/SiO2 sphere, where the silica part is completely immersed in the water phase due to its hydrophilicity, while Pt is located in the n-decane phase.28 This leads to the Janus boundary assuming a horizontal position along the liquid–liquid interface and, therefore, no propulsion. However, when the top and bottom phases of the LLI are swapped by flipping a specially designed microscopic cell so that the top phase is an aqueous hydrogen peroxide solution instead of a commonly lighter oil, the Janus particle initially dispersed in the hydrogen peroxide phase is not trapped at the LLI but propels slightly above it. A similar observation was made for the propulsion of Janus particles in the presence of oil droplets engineered by microfluidics.29 Moreover, the experimentally observed contact angle and orientation of Janus colloids also greatly depend on their surface roughness (besides their surface chemistry), which leads to an observed pinning of the three-phase contact line in non-equilibrium positions and a variety of orientations.30
Studies on the propulsion of self-diffusiophoretic and self-electrophoretic Janus particles at the liquid–fluid interface are very limited, with only a few examples of propelling systems so far. Self-propulsion at air–water interfaces is typically characterized by large velocities, which surpass the velocity of Janus particles near a solid wall.31,32 For example, a carbon fiber functionalized with glucose oxidase and bilirubin oxidase propels with velocities between 10−3 and 10−2 m s−1 at the interface between air and an aqueous D-glucose solution, which is related to the small viscous drag at the air–water interface as well as to large electric currents generated by the enzymatic reactions.31 A two-fold increase in velocity compared to the propulsion in the bulk was also observed for Pt/SiO2 spheres at the air–water interface.32 Surprisingly, the more a Janus particle is immersed in the aqueous phase the faster it moves, which is a consequence of the random thermal fluctuations of the contact line between the particle and the air–water interface, leading to additional forces exerted on the particle.33,34
An opposite trend was shown by Dietrich et al.30 for Pt/PS self-diffusiophoretic spheres propelling at the interface between hexadecane and an aqueous solution of hydrogen peroxide. The velocities of these Janus particles were smaller than the velocities of the same particles propelling near a solid wall because of the larger viscosity of hexadecane. The dependence of the self-diffusiophoretic velocity of Janus particles near a fluid–fluid interface on the viscosity ratio between the two fluids was also described theoretically by several groups.35–37 In particular, a non-zero viscosity difference leads to the emergence of a torque and particle rotation around the axis parallel to the LLI.37 At diminishing viscosity differences, rotational and translational velocity are reduced to their respective components in the bulk. However, it should be noted that these calculations are made with the assumption that both reactants and products can freely diffuse in both phases, which does not hold for the oil component.37 Pt/Au nanorods propelling parallel to their long axis at the water/n-decane interface were also studied experimentally,38 with more focus, however, on assessing the possibility of using them for the precise measurement of the surface shear viscosities by varying the concentration of surfactants dispersed in the aqueous phase.
A mechanism of Janus particle propulsion at the LLI was suggested for self-diffusiophoretic Pt/PS spheres by Dietrich et al.30 According to their findings, the orientation of the platinum and polystyrene sides of the particle at the LLI dictates the strength of the interfacial chemical gradient, leading to a bimodal distribution of particle velocities. In particular, the more the catalytic side is submersed in the hydrogen peroxide phase, the less steep the gradient created along the LLI, resulting in smaller particle velocities.
The current study aims to expand the description of Janus particles at the LLI between an aqueous solution of hydrogen peroxide and oil beyond spherical geometries. We consider sideways propelled Pt/Au Janus particles, which, in contrast with previously studied systems, move by self-electrophoresis. This geometry can be beneficial for a range of applications where a larger active surface area is needed, in particular, for collection and transport of microscopic cargo.39–42
The monolayer of PS fibers was sputter-coated (Quorum, Q150TS) with ∼20 nm thick Pt/Pd and Au/Pd layers on opposite sides of the monolayer respectively, resulting in long Janus fibers. For simplicity these coatings will be referred to as Pt and Au coatings in this paper. For the preparation of the Janus rods, the Janus fibers were dispersed in liquid medium and cut into smaller rods of 10–100 μm length by ultrasonication using an ultrasonic probe (Hielscher UP400S, the total power 450 W) for 1.5 min. For the preparation of Janus rods for the measurements of a its velocity in 5 wt% H2O2 near a solid–liquid interface at the bottom of a microscopy cell, also referred to here as a solid wall, the fibres are dispersed in water. The separation distance between the rod and the solid wall is approximately 550 nm.39 For liquid–liquid interface (LLI) experiments, the Janus fibers were dispersed in isopropanol (IPA):
water (2
:
3) solution prior to ultrasonication. Ultrasonication results in rods with a broad length distribution and bent rods.
The sideways self-propulsion of Pt/Au rods at the LLI between an aqueous solution of hydrogen peroxide (5 wt%) and n-decane was captured with an inverted optical microscope (Olympus, IX71) with a 10× objective. The videos were then analyzed with a custom-written Python code to determine the particles trajectories and velocities.‡ The rod velocities were extracted from their displacement via image processing from the movies and averaged over the multiple consecutively captured frames. Decomposition of hydrogen peroxide gives rise to an additional displacement of particles in the microscopy cell due to convection, which was determined from the apparent motion of immobile particles and subtracted from the displacement of self-propelled rods.
![]() | (1) |
The cell is sealed with a cover glass to reduce convection, which is, however, still present to a limited degree due to hydrogen peroxide decomposition and production of oxygen bubbles. These oxygen bubbles are trapped at the LLI due to capillary forces that counteract the buoyancy force and prevent them from crossing the LLI.48
Fig. 2 shows the typical motion of a Janus rod at the LLI (additionally, see Movie M1 in the ESI†).
![]() | ||
Fig. 2 Sideways propelled Pt/Au rod at the interface between an aqueous hydrogen peroxide solution (5 wt%) and n-decane, scale bar is 30 μm. |
The velocities of the sideways propelled Janus rods at the LLI shown in Fig. 3 are larger than their velocity of 1.82 ± 0.18 μm s−1 near a solid wall due to the smaller drag at the LLI. Note that the absolute viscosity of n-decane at room temperature ηd = 0.84 mPa s is close to that of water ηw = 0.89 mPa s,49 which explains the apparent discrepancy of this result to the dynamics of Pt/PS spheres studied at the water/hexadecane interface.30 Since the viscosity of hexadecane ηh = 3.06 mPa s is three times larger than that of water,49 particles at the water/hexadecane interface experience an increased viscous drag, resulting in a lower velocity than that observed near the wall. As shown in Fig. 3A, the velocity of the Janus rods does not depend on the rod length, which is in agreement with a study of the sideways motion of Janus rods near a wall.41 Moreover, the velocity of a single rod is stable during the measurement time, indicating no rotation around its long axis.
![]() | ||
Fig. 3 (A) Velocities of Pt/Au sideways propelled rods at the interface between aqueous hydrogen peroxide (5 wt%) and n-decane vs. their lengths (over 21 rods). (B) The probabilities p(v) of observing rods with velocities v. For clarity, velocities v that were in the range of ±10% from each other were combined together (resulting in 2, 8, 8, 4, and 1 rods per respective data point in the figure). Red dashed line: mean velocity of the rods near a wall; the red area represents the standard deviation. (C) Schematic of the proposed mechanism of the Pt/Au Janus rod propulsion, based on the studies of Dietrich et al.30 The upper yellow phase is n-decane and the bottom blue phase is an aqueous solution of 5 wt% H2O2. |
A significant difference in the Janus rod propulsion at the LLI when compared to their motion near a solid wall is the much wider distribution of the observed velocities. Most of the Pt/Au rods have a velocity in the range of 5–10 μm s−1, with smaller fractions moving at velocities up to 16 μm s−1 and 2–5 μm s−1. A similar tendency was also noticed for Pt/PS spherical particles at the LLI, which, however, have only two distinct sets of velocities, emerging from two prevailing particle orientations.30 The term orientation here refers to the particular configuration of a Janus sphere or rod at the LLI, depending on how the boundary between the two metals (or the metal and the insulator) pierces the interface. It was shown that different orientations of a Janus particle give rise to concentration gradients of different strengths along the LLI, resulting in slower and faster sets of propelling particles.30 For bimetallic Janus rods, we suggest a similar reason for the large distribution of velocities. The difference is, however, the mechanism of particle motion that dominates. There is strong evidence that bimetallic particle propulsion in hydrogen peroxide is induced by self-electrophoresis. According to this mechanism, Pt/Au particle motion is driven by a self-induced electric field due to electrochemical half-reactions occurring on Pt and Au:50,51
Pt (anode): H2O2 → O2 + 2H+ + 2e− | (2) |
Au (cathode): H2O2 + 2H+ + 2e− → 2H2O | (3) |
Overall: H2O2 → O2 + 2H2O | (4) |
Platinum and gold coatings act as an anode and cathode, respectively, producing an inhomogeneous distribution of protons along the particle surface. These protons are known to adsorb at air–water and oil–water interfaces,52 which decreases their surface tension and modifies the ζ-potential. In particular, at pH ≈ 2–3 a number of liquid–fluid interfaces, including water/oil interfaces, have zero ζ-potential, which decreases with the increase of pH and for many water–oil systems equals ζ ∼ −30 mV at pH ≈ 4 (value for 5 wt% H2O2).53 An inhomogeneous release of protons thus leads to a similar phenomenon as for self-diffusiophoretic Pt/PS particles, where the difference in propulsion velocities stems from the variation in electric field strength for different orientations of the rods as shown in Fig. 3C and not from concentration gradients. Note that in contrast to Pt/PS spheres,30 only a fraction of the bimetallic Pt/Au rods propel. This is likely stemming from the larger number of bimetallic rods that have the contact line pinned at only one Janus side (as depicted in Fig. 3C, bottom image) compared to Pt/PS spheres. This configuration does not result in a self-induced electric field and is, therefore, immobile.
The self-propelled velocities of the particles at the LLI are found to be up to 8 times larger than their velocities near a solid wall, which can only be partially explained by the decreased viscous drag at the LLI compared to a solid boundary. Indeed, as pointed out by Wang et al.,54 a particle's mobility near the LLI can be increased by reduced drag only by up to 3 times compared to that at a solid–liquid interface. We hypothesize that the enhancement in velocity is related to electrokinetic effects that is for example not present in catalytic systems where the motion does not stem from a self-induced electric field.30 In particular, electroosmotic flow at the solid–liquid interface is known to decrease the velocity of self-electrophoretic particles by up to 25% compared to their bulk velocity.55
To calculate the thermodynamically favorable configuration of Janus rods at the LLI, defined by angles α and β in Fig. 4A, the wetting properties of rod's opposing surfaces need to be assessed. Macroscopic contact angles are measured for a water drop in n-decane on bare PS (ΘPS = 144.5° ± 3.8°), on PS coated with Pt (ΘPt = 93° ± 2.4°) and PS coated with Au (ΘAu = 101° ± 4.9°). Due to the small difference between ΘPt and ΘAu, there is no preferential equilibrium orientation, and the angle α in Fig. 4A cannot be evaluated theoretically. However, the existence of a range of observed rod velocities suggests that, similarly to the study of Pt/PS spheres,30 sideways propelled Janus rods are pinned at the LLI in different orientations due to their surface roughness.56 For Pt/PS spheres, as discussed by Dietrich et al., the particle orientations are truly metastable and different from the thermodynamically favorable one, while for Pt/Au rods no equilibrium configuration can be derived due to the fact that the contact angles for both metals are nearly identical.
The contact angles were also measured after placing the Pt/PS and Au/PS plates in H2O2 for 5 min. This allows us to determine and compare the equilibrium position of Janus rods both for the initial coating and after its exposure to hydrogen peroxide solution. Noble metals are known to considerably adsorb airborne hydrophobic contaminants, which results in larger contact angles, while the clean surfaces are usually more hydrophilic.57 Hydrogen peroxide, being an oxidizer, is expected to clean the surface of the metals and thus decrease the measured contact angles. The resulting contact angles after exposure to H2O2 are in fact smaller and equal to ΘPt,H2O2 = 58° ± 6.5° and ΘAu,H2O2 = 65.4° ± 3.7°.
The angle β and thus the protrusion height h are then derived by finding the minimum of energy:
ΔE = E − E0, | (5) |
E = γPt,dAPt,d + γPt,wAPt,w + γAu,dAAu,d + γAu,wAAu,w + γw,dAw,d − γw,dAint, | (6) |
E0 = πrL(γPt,d + γAu,d) + γw,dAw,d, | (7) |
The end of the Janus rod, where PS is exposed to both liquids, is not taken into account, since its area is relatively small compared to the overall surface of the Janus rod and does not have a significant influence on the obtained protrusion height. The theoretical protrusion height h for each rod diameter is visualized in Fig. 4B, both for the initial hydrophobic Pt and Au surfaces (solid line) and after their exposure to hydrogen peroxide (dashed line).
The real protrusion height of the Janus rods at the LLI was studied experimentally by AFM after trapping the particles in a PDMS layer. Fig. 4C shows an example of a Janus rod measured by AFM, for which the protrusion was calculated as the maximum height along the white line. As shown in Fig. 4B, the experimental data is close to the theoretical protrusion height of the neat metal surfaces, and differs from the theoretically calculated protrusion height after exposure to hydrogen peroxide. One of the reasons why the influence of H2O2 on the contact angle of a Janus rod is negligible could be the use of IPA:water as the spreading solution to distribute the particles at the water/n-decane interface, which can become trapped in metal surfaces heterogeneities.58 Janus rods protrude more into the n-decane phase than into the aqueous phase. The large variability in the data is possibly the result of the multi-step gel trapping technique as well as the preparation procedure of the Janus rods.
To explain the large variation of velocities in Fig. 3A and B, we measured the orientation of Janus rods at the n-decane/water interface, defined by the angle α, using SEM EDX. Since the M lines in the EDX spectra of Pt and Au are not well-separated, an Ag coating, which has similar wetting properties as Pt,59 was sputtered instead. Line scans along the diameter of the rods trapped in PDMS in the same configuration as at the n-decane/water interface revealed that most Janus rods have their boundary between the two metal coatings oriented horizontally along the n-decane/water interface. This configuration induces a homogeneous distribution of the reaction products at the oil/H2O2(aq.) interface and thus does not lead to propulsion, as, in fact, observed for the majority of the rods (Fig. 3). As shown in Fig. 5C, a smaller fraction of Janus rods has their boundary between the two metal coatings piercing the interface at different angles. Fig. 5D shows an elemental map of a Janus fiber observed from the oil side. The majority of these configurations has equal Ag(Pt) and Au surface areas in both phases, while smaller fractions have one of the metals oriented more to the hydrogen peroxide phase. According to Dietrich et al.,30 a larger velocity is induced by the configuration which produces steeper chemical gradients at the oil/water interface. Since the motion of Pt/Au relies on the gradient of protons produced on the platinum side, we expect that a Janus rod with less Pt in the hydrogen peroxide phase moves faster than those with a larger part of Pt in the hydrogen peroxide phase. Therefore, presumably, a rod with a smaller gold fraction in n-decane (and thus a smaller Pt fraction in water) induces a velocity larger than ∼8 μm s−1, while a rod with more gold coating in n-decane induces a velocity smaller than 8 μm s−1. The intermediate configuration with equal parts of both metals in hydrogen peroxide solution is thus expected to result in intermediate velocities around 8 μm s−1. As shown in Fig. 3, the probability of observing rods with this velocity is the largest across the velocity range, which is in good agreement with a larger probability of observing the intermediate configuration (Fig. 5C). Moreover, the propulsion experiments performed on Pt/PS rods indicate that the mechanism of propulsion is not influenced by the shape of the particle but solely by its orientation at the LLI. As shown in Fig. 6A, the velocities of Pt/PS rods are similar to Pt/PS spheres,30 with two distinct sets of slower and faster particles. The presence of two preferred orientations of the rod, corresponding to a smaller and larger Pt part in the aqueous phase was also confirmed by SEM EDX analysis in Fig. 6B. Note that Pt/Au rod velocities at the LLI can be up to 8 times larger than their velocities near a wall, while the increase in the velocity of Pt/PS rods is only a factor two to three.
Finding a direct link between the orientation of a bimetallic Janus rod and its velocity, both measured in situ, is a promising direction to further understand its mechanism of propulsion, which is, however, outside of the scope of the current work.
Our study, therefore, provides an experimental basis to modulate the propulsion of bimetallic anisotropic particles by trapping them at liquid–liquid interfaces.
Footnotes |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d3sm00466j |
‡ The Python code for the tracking of the rods motion: https://github.com/ReknowIndra/rod-track. |
This journal is © The Royal Society of Chemistry 2023 |