Abstract
Catalytic micromotors can be used to detect molecules of interest in several ways. The straightforward approach is to use such motors as sensors of their “fuel” (i.e., of the species consumed for self-propulsion). Another way is in the detection of species which are not fuel but still modulate the catalytic processes facilitating self-propulsion. Both of these require analysis of the motion of the micromotors because the speed (or the diffusion coefficient) of the micromotors is the analytical signal. Alternatively, catalytic micromotors can be used as the means to enhance mass transport, and thus increase the probability of specific recognition events in the sample. This latter approach is based on “classic” (e.g., electrochemical) analytical signals and does not require an analysis of the motion of the micromotors. Together with a discussion of the current limitations faced by sensing concepts based on the speed (or diffusion coefficient) of catalytic micromotors, we review the findings of the studies devoted to the analytical performances of catalytic micromotor sensors. We conclude that the qualitative (rather than quantitative) analysis of small samples, in resource poor environments, is the most promising niche for the catalytic micromotors in analytical chemistry.
1. Introduction
Catalytic micromotors are micrometer-sized objects which self-propel when the solution in which they are suspended contains species which they can chemically convert. It is important to note that in order to achieve self-propulsion, the object should be, in general, sufficiently asymmetric either in shape or/and in the surface distribution of the catalytic processes (e.g., only on half of a spherical microbead, see Figure 1) such that a preferred direction can be defined. (The breaking of the isotropic symmetry, which is necessary for motion, can also be induced by boundaries; e.g., a spherical catalytic particle near a wall would exhibit motion in the direction normal to the wall.) While at short times the motion of a typical micromotor is ballistic, at long times it crosses over to Brownian motion, albeit with an effectively enhanced diffusion coefficient that depends on the activity of the particle [1].
The first catalytic micromotors were reported in 2004: bimetallic nanorods (1–2 µm long, ~200 nm in diameter, half Au and half Pt), which self-propelled by catalyzing the decomposition of H2O2 [2]. This report has been followed by intense research efforts aimed at, among others: determining the mechanism of propulsion [3,4], the development of micromotors propelling with other “fuel” than H2O2 [5,6,7], controlling the trajectory of the micromotors [8,9,10], and, obviously, related to the question of applications for catalytic micromotors [11,12]. The efforts aimed at determining the mechanism of propulsion, for example, have shown that self-propulsion can occur via self-diffusiophoresis [1], self-electrophoresis [3,4], or bubble ejection [13].
Figure 1.
(A) Schematic representation of a Janus-type catalytic micromotor self-propelling by the photochemical decomposition of H2O2 in the vicinity of a wall; (B) Calculated concentration gradients produced by a Janus-type catalytic micromotor in the vicinity of a wall (color coded, in arbitrary units) superimposed over calculated hydrodynamic flows produced by such a catalytic micromotor (streamlines, white); Figures reproduced with permission from Ref. [14].
One very promising application of catalytic micromotors is in analytical chemistry, in the detection and quantification of different molecules of interest in food, environmental, or clinical samples. Catalytic micromotors can be used to detect molecules of interest in several ways (see also Figure 2). The most straightforward way is to use the micromotors to detect their “fuel” (i.e., the species they are consuming for self-propulsion) (see Figure 2A). This approach requires the motion of the micromotors to be carefully analyzed (using a microscope, a digital camera, and the appropriate software tools) because the speed (or the diffusion coefficient) of the micromotors, which depends on the concentration of the analyte of interest, is the analytical signal. Another possibility is to use the micromotors to detect species which do not act as fuel for the micromotor but still can modulate (e.g., inhibit, activate, etc.) the catalytic processes facilitating self-propulsion. This approach also requires an analysis of the motion of the micromotors because the speed (or diffusion coefficient) of the micromotors remains the useful analytical signal. Finally, catalytic micromotors can also be used as tools for enhancing the mass transport (and the probability of specific recognition events) in the sample. This approach is based on “classic” (e.g., electrochemical, fluorescent, etc.) analytical signals and does not require an in-depth analysis of the motion of the micromotors (see Figure 2B).
Figure 2.
Two ways of using catalytic micromotors for sensing. (A) Fuel molecules (or species which inhibit/activate the catalytic process) are the analytes of interest and either the speed or the diffusion coefficient of the catalytic micromotors is the analytical signal; (B) The self-propulsion of the catalytic micromotors has the role of increasing mass transport within the investigated sample (by inducing flow of the solution and by moving through the solution). The catalytic micromotors carry classic biomolecule detection schemes (such as the “sandwich-type” detection scheme based on antibodies schematically shown here). Depending on the detection scheme, in this approach, the analytical signal is either optical or electrochemical.
Catalytic micromotors are often obtained by complicated, multistep procedures. Many of them also rely on rather expensive materials (e.g., noble metals, purified enzymes, antibodies, etc.). Cost-effective mass production of highly reproducible catalytic micromotors is still a problem in spite of improvements brought about by, for example, Pickering emulsion-based methods [15,16]. Why are catalytic micromotors still interesting for sensing in such conditions? There are several features which recommend catalytic micromotors for sensing:
- (i).
- First, catalytic micromotors can analyze tiny samples. They can be suspended and their motion investigated in few microliters of sample. This is useful when large volumes of samples are not available (e.g., blood samples collected from very low birth weight infants [17,18,19]). One should also note that the ability to work with small samples advantageously translates into smaller amounts of chemical/biological waste.
- (ii).
- Second, catalytic micromotors (via their motion) can facilitate enhanced mass transport within the investigated sample without using laboratory equipment (such as stirrers, vortexes, or pumps). This can be important for investigations carried out outside specialized laboratories, in remote areas with limited resources. It can also be important when analyzing a few microliters of sample (e.g., a drop of blood, sweat, tear, or saliva placed on a microscope glass slide). There are very few tools for stirring/mixing within tiny liquid droplets.
- (iii).
- Third, the signal of the catalytic micromotors can be documented using a mobile phone instead of a bulky, expensive laboratory equipment. In turn, this can facilitate sensing outside specialized laboratories and, eventually, by untrained users. While this possibility represents an advantage over classic analytical approaches (which most often require bulky and expensive instrumentation that is used by trained staff in specialized laboratories), only a few times it has been demonstrated. Both the collective behavior of catalytic micromotors [20] and the individual behavior of catalytic micromotors [21,22,23] were already documented using mobile phone cameras and linked to the concentration of the analyte of interest. Reading the fluorescence of catalytic micromotors using a mobile phone was also recently reported [24]. Important to note, some of these mobile phone-based approaches to study micromotors are still relying on image analysis carried out on a computer.
- (iv).
- Forth, sensing with catalytic micromotors is characterized by high spatial resolution because each tiny motor reports on the concentration of the analyte in the solution adjacent to the micromotor. However, achieving sensing with high spatial resolution (i.e., building high resolution chemical 2D/3D maps with catalytic micromotors) is currently still hindered by the heterogeneity of the catalytic micromotors. One cannot be 100% sure that a micromotor self-propels faster/slower than the other because of the local availability/unavailability of the targeted analyte or because of intrinsic, but yet not well understood, heterogeneity from batch to batch, or even within the same batch, in the properties of the individual micromotors (see also Section 2), or for various other reasons related to the experimental setup. For example, it has been observed that hydrazine-fueled micromotors propel faster at the edges of a water droplet than in the middle of it, immediately after the droplet is exposed to hydrazine vapors [25]; this is so because in that setup the hydrazine vapors reach the micromotors faster through the shallow edges of the water droplet [25].
- (v).
- Last but not least, catalytic micromotors can combine sensing with other functions (e.g., with neutralization of dangerous chemicals). However, this possibility was also seldom explored. Metal ions were both detected and collected/removed using some H2O2-propeled catalytic micromotors [26,27].
The above advantages (or possible advantages) of catalytic micromotors as sensors are currently explored by research groups worldwide and were highlighted in a good number of papers. The present (focused and thorough) overview of the catalytic micromotors used to detect and quantify analytes of interest complements several recent reviews about sensing with micromotors [28,29,30,31,32,33,34,35,36,37].
2. The Speed (or Diffusion Coefficient) of Catalytic Micromotors as Analytical Signal
When considering potential ways to employ catalytic micromotors as sensors, it is intuitively appealing to attempt exploiting the dependence of the speed (or, alternatively, the effective diffusion coefficient) of the micromotor on the presence of the analyte of interest. This dependency can occur in several scenarios. The analyte of interest can be the reactant in the catalytic process responsible for the self-propulsion, that is, the analyte of interest acts as fuel for the catalytic micromotors. For example, micrometer sized objects modified with enzyme were used as sensors for the substrate of the respective enzyme [6,38]. The analyte of interest can be an inhibitor or activator of the catalytic process responsible for self-propulsion. For example, Au-Pt bimetallic nanorods were used to detect Ag+ ions as these ions activated the decomposition of H2O2 self -propelling such nanorods [39]. Finally, in certain situations, the analyte of interest can slow down the micromotor despite limited (or no) impact on the catalytic process responsible for self-propulsion. For example, the already mentioned Au-Pt nanorods were observed to be slowed down by common ions in rather low concentrations because ions impact the reaction-induced self-generated electric field [39,40].
In the following, we focus, for simplicity, on the case of self-phoretic spheroidal catalytic micromotors (see Figure 3A), with the analyte of interest being the reactant in the first-order chemical reaction powering the micromotor.
Figure 3.
(A) Schematic representation of spheroidal catalytic micromotors characterized by the same polar semi-axis (R1), different equatorial semi-axes (R2), and, thus, different aspect ratios sr = R2/R1. (Obs.: The part of the catalytic micromotor covered by catalyst, that is, the active cap of the catalytic micromotor, is depicted as a black area). (B) The dependence of the scaled phoretic velocity (Vpr/V0) on the fraction of the surface of the catalytic micromotor covered by the catalyst (η0 = −1, 0, 1, respectively, correspond to a micromotor surface with no catalyst, with the lower half covered by the catalyst, and completely covered by the catalyst, respectively), for a prolate-shaped spheroidal catalytic micromotor with aspect ratio parameter ξ0 = (1 − sr2)−1/2 = 80 (sr = 0.9999), 2 (sr = 0.866), 1.1 (sr = 0.42), 1.01 (sr = 0.14), and 1.005 (sr = 0.099). The large ξ0 values correspond to a quasi- spherical shape, while the limit towards 1 corresponds to needle-like shapes (approximating a long rod). Figures reproduced with permission from Ref. [41].
One notes that from a theoretical perspective, this set-up seems optimal, in that the speed is maximal at half-coverage of the micromotor with catalyst (see Figure 3B). The speed is also quite robust against fabrication defects, if the axial-symmetry is preserved: the speed maximum is relatively flat with respect to the coverage, and thus variations in coverage have small influence on the value of the speed [41]. Furthermore, in the range of few micrometers of sizes, and for first-order kinetics of the catalytic chemical reaction, the self-phoretic speeds are independent of the size of the particle [1].
Using a spherical shape as an example, the arguments above can be made more quantitative in that the speed V, as a function of the coverage θ (the angle between the axis of the particle and the rim of the active cap; it runs from 0, for zero coverage, to π, for a fully covered sphere) by the catalyst, is given by V = (1 – cos2θ) V0 (where V0 ~ C is a characteristic velocity directly proportional with the concentration C of fuel and, in a first-order approximation, independent on the size of the particle). Thus, in order to see, for example, a change in velocity by 10% from the nominal value at θ = π/2, which is the case of a Janus particle, the coverage θ’ should change to the one obeying cos2θ’ = 0.1, i.e., θ’ ≈ 0.4 π. This is a rather large variation, and most of the modern methods of manufacturing Janus colloids can perform better than that without particular technical demands.
Although the theoretical point of view suggests a robust operation of Janus particles as motors, there is an increasing body of experimental evidence that there must exist additional parameters, beyond the geometrical aspects discussed above, that play an important role in the emerging motion. For example, for seemingly identical TiO2 on SiO2 Janus-type motors (with radius of 275 ± 8 nm), the active velocity is measured by Sachs et al. [42] to be a stochastic variable with a quasi-Gaussian distribution of a width comparable to the average value (7.9 µm/s; see Figure 4A).
Figure 4.
(A) Velocity distributions for TiO2 on SiO2 Janus-type motors (d ~550 nm) in 2.5% H2O2; (B) Velocity distribution for Pt on polystyrene Janus-type motors (d ~2.8 µm) in 0.1% (top), 1.0% (center) and 3.0% (bottom) H2O2; (Obs.: (A) is built using the average speed of individual motors while (B) shows experimental velocity distributions for ~30 individual micromotors). Figures reproduced with permission from Ref. [42] (panel (A)) and Ref. [43] (panel (B)).
Similar findings are reported for nanorods (either classic Au-Pt or the more rapidly moving ones made with carbon nanotubes) [44], as well as for a variety of other types of Janus spheres in aqueous solutions of H2O2 [43,45] (see Figure 4B). In all cases, this has been attributed to an intrinsic variability of the catalytic activity of the materials, but why this is happening, and how can it be controlled, remains thus far unclear. The impact of such large dispersion around the average value as in the data in Figure 4A is dramatic in what concerns the accuracy of an analytic method based on the value of the velocity (which, in the first approximation, is proportional to the fuel concentration): a change in the velocity from the average value of ~8 µm/s by a standard deviation of ~2 µm/s represents a 25% variation which, unknowingly, would render an over (or under) estimated fuel concentration by the same percentage.
The experimentally observed variability of the speed of catalytic micromotors impacts also the way catalytic micromotors are used as sensors. It is clear that the speed of a large sample of micromotors must be averaged into an average speed both during the calibration of the micromotors with solutions containing known concentrations of analyte and during the analysis of samples of unknown chemical composition. Only such average speeds will reflect the correct analyte concentration in the standard solutions and investigated samples. The wider the distribution of self-propulsion speeds, the larger the number of micromotors which must be analyzed for correct results. Analyzing the speed of large numbers of micromotors requires time, careful experiments (e.g., the experiments must have an optimal number of micromotors in the field of view, the micromotors must stay long enough in the field of view, etc.), and also important computing power. The experimentally observed variability of the speed also compromises the idea of using catalytic micromotors for sensing with spatial resolution (an idea that is based on the assumption that all catalytic micromotors taken into work are characterized by similar parameters of the motion in similar experimental conditions).
In spite of the above-described complication, the first studies exploring catalytic micromotors as sensors did use the speed (or the diffusion coefficient) of the micromotors as the analytical signal (see, for example, [39]). Therefore, the following two sections will shortly review catalytic micromotor sensors which report on the concentration of the analyte of interest via the parameters of their motion. As we will see, the analyte of interest is either the fuel of the catalytic micromotors (Section 3) or a molecule which modulates the catalytic process without being the fuel of the catalytic micromotors (Section 4).
3. Sensing Analytes Which Are Also Fuel for the Catalytic Micromotors
Most catalytic micromotors developed up to now use H2O2 as fuel. These H2O2-fueled micromotors have been reported to exhibit dependence of the velocity on the concentration of H2O2. For example, already the first catalytic micromotors, developed by Paxton et al., self-propelled at speeds of 3.9 µm/s in 0.03% H2O2 and at speeds of 7.9 µm/s in 3.3% H2O2 [2]. Ni on Pt microtubes (L ~10–20 µm, ϕ ~2–3 µm) were shown to self-propel at speeds of 75 µm/s in 1% H2O2 and at speeds of 165 µm/s in 5% H2O2 [46]. Polycaprolactone microspheres (d ~30–40 µm) carrying MnO2 particles were also shown to self-propel at speeds of 15 µm/s in 5% H2O2 and at speeds of 43 µm/s in 25% H2O2 [47]. As a consequence of this repeatedly documented dependence, the idea of using catalytic micromotors as sensors for the quantification of their fuel molecules has emerged. However, a convincing practical implementation of the idea was slowed down by several findings. Particles presumably moving by self-electrophoresis or self-diffusiophoresis (two mechanisms of self-propulsion) were found to be very sensitive to the presence of ions in the solution, which is actually a ubiquitous feature in most real-world samples [39,48]. The speed of catalytic micromotors was found to disadvantageously depend on the sample matrix as well. For example, Mg-based catalytic micromotors (which self-propel by ejecting H2 bubbles in H2O, a mechanism considered more robust than self-phoresis) were found to self-propel with speeds of 296 ± 40 µm/s in water, 223 ± 38 µm/s in whiskey, 108 ± 18 µm/s in milk, and only 40 ± 8 µm/s in serum at the same H2O2 concentration [49]. The speed of catalytic micromotors was found to depend significantly also on the working temperature. For example, the speed of Pt-based rolled-up microtubes (self-propelling due to the O2 bubbles produced in 1% H2O2) was found to be ~400 µm/s at 20 °C and ~550 µm/s at 25 °C [50]. These additional dependencies (of the self-propulsion speed on sample features which are not always easy to control) very much weaken the robustness and reliability of catalytic micromotors as analytical tools. They add to the already mentioned problem related to the variability of the speed of self-propulsion for seemingly similar catalytic micromotors (Section 2).
The few studies in which catalytic micromotors are used as sensors for the detection of their fuel are shortly presented in Table 1. As highlighted in the table, the catalytic micromotors used to sense their fuel self-propel by either self-diffusiophoresis or self-electrophoresis. The fascinating details of these two mechanisms are nicely presented in a review by Moran and Posner [40].
Table 1.
Examples of catalytic micromotors which were used to detect/quantify their fuel. (Used abbreviations: GOx = glucose oxidase, GluOx = glutamate oxidase, XOD = xanthine oxidase, DL = detection limit, and LR = linear range).
Figure 5 completes Table 1 and shows typical calibration curves which link the speed (or the diffusion coefficient) of the micromotors to the concentration of the fuel (i.e., analyte of interest). On one hand, the rather similar calibration curves obtained in water and serum (see Figure 5A) argue that enzyme-based micromotors can be used for sensing in relatively complex samples, such as 10× diluted serum. On the other hand, these calibration curves also highlight yet another difficulty in using enzyme-based micromotors to detect their fuel molecules: the dependence of the speed (or the diffusion coefficient) of the micromotors on the concentration of the fuel is linear for a very narrow range of concentrations. (Moreover, in the case of GOX-based micromotors, there is the additional complication of the re-entrant behavior, i.e., for a range of increases of the diffusion coefficient, there are two possible values of the substrate concentration for each specific value of that increase.) The samples to be investigated must be diluted or preconcentrated in order to fit that range. However, while not convenient, this is not something unusual with other analytical tools as well.
Figure 5.
(A) The dependence of the relative diffusion coefficient of XOD-modified nanorods and of GOx-modified nanorods on the concentration of hypoxanthine and glucose, respectively, in water and in 10× diluted serum; (B) The dependence of the reaction rate (in blue) and of the self-propulsion speed (in red) of silica microcapsules modified with urease on the concentration of urea in water; Figures reproduced with permission from Ref. [6] (panel (A)) and from Ref. [38] (panel (B)).
4. Sensing Analytes Which Modulate the Speed of Self-Propulsion without Being Fuel for the Catalytic Micromotors
As noted in the previous section, catalytic micromotors were used only a few times to detect analytes which also act as fuel for them. We have discussed a number of complications which seem to explain the limited popularity of that approach. However, catalytic processes can be slowed down or accelerated by certain species other than their reactants, and the catalytic processes which self-propel the catalytic micromotors make no exception from this rule. This opens the possibility to use catalytic micromotors also for the detection of these inhibitors and activators. As another possibility, catalytic activity (instead of being slowed down by inhibitors or accelerated by activators) can be conferred to microstructures (e.g., a microtube) from scratch, via biorecognition events selective for the analyte of interest. This approach was used to detect DNA, for example (see details in [51]). The detection required microtubes to be modified with capture DNA. When the target DNA was available in the investigated sample, the modified microtubes were able to bind not only target DNA but also detector DNA that was previously labeled with Pt nanoparticles. The latter, together with H2O2 as fuel, put the microtubes into motion with speeds which were proportional with the concentration of DNA target in the sample (see Figure 6). Catalytic micromotors facilitated not only this “signal on” (or OFF-ON) type biosensing concept but also “signal off” (or ON–OFF) type detection concepts (see, for example, in Ref. [52]). As a final possibility, one can exploit the fact that accumulation of antibody–antigen–antibody complexes on the surface of catalytic micromotors can slow down the self-propulsion of catalytic micromotors by attaching significant weight to the catalytic micromotors [53].
Figure 6.
(A) Modification of the inner surface of poly(3,4-ethylenedioxythiophene) (PEDOT) on Au microtubes with capture DNA, and of Pt nanoparticles with detector DNA; (B) The principle for DNA detection by introducing Pt nanoparticle-DNA conjugates into the microtubes via specific DNA hybridization mediated by target DNA; Figure reproduced with permission from Ref. [51].
A summary of the studies employing catalytic micromotors to detect species which modulate the speed of the self-propulsion without being fuel for the catalytic micromotors is presented in Table 2.
Table 2.
Examples of catalytic micromotors which were used to detect analytes which modulate the speed of self-propulsion without being fuel for the catalytic micromotors; (Used abbreviation: BSA = bovine serum albumin).
There are several interesting points one can make based on Table 2. Most catalytic micromotors listed in Table 2 self-propel by the O2 bubbles generated by the decomposition of H2O2 and not the phoretic mechanisms mentioned in Section 3. This mechanism of self-propulsion was most probably preferred due to its relative insensitivity to common ions. Bubble-propelled catalytic micromotors were already tailored for the detection of a wide range of analytes, such as small metal ions (e.g., Hg2+), nucleic acids (e.g., DNA), proteins (e.g., carcinoembryonic antigen), viruses (e.g., Zika virus), and small organic compounds (e.g., glutathione). Most catalytic micromotors listed in Table 2 use the speed of self-propulsion as the analytical signal. However, this speed can be replaced with the distance traveled by the catalytic micromotors as the analytical signal. Such a switch, from speed to distance, was already done for the detection of DNA [59].
On the other hand, the drawbacks and problems of the catalytic micromotor sensors mentioned in Section 3 are carried over also to the catalytic micromotor sensors listed in Table 2. Using the speed of catalytic micromotors as the analytical signal still requires highly reproducible micromotors (as slightly different motors will report slightly different concentrations of the targeted analyte) and obtaining highly reproducible micromotors is still very difficult. For example, the average speed of some catalytic micromotors used to detect DNA in the nM range was reported to be 418 ± 25 μm/s [52], while such a standard deviation corresponds to tens of nM of DNA. pH sensitive catalytic micromotors were observed to self-propel at speeds in between 70 µm/s and 110 µm/s at the same pH of the solution [57]. Such a difference in the speed of self-propulsion (40 µm/s) corresponds to roughly 2 pH units. Averaging the speeds of several catalytic micromotors is clearly needed in order to correctly determine the concentration of the targeted analyte in a sample. As already pointed out, averaging is time consuming (as several trajectories need to be analyzed) and compromises the possibility of using catalytic micromotors for biosensing with high spatial resolution. Micromotors listed in Table 2 are still significantly slowed down in complex media, such as cell culture media, serum, or whole blood. For example, poly(aniline) on Pt microtubes were observed to self-propel with speeds of 140 μm/s in buffer solution with 1.2% H2O2 and with speeds of 90 μm/s in serum with 1.2% H2O2 [53]. The slowdown, when operating in serum, was speculatively attributed to the higher viscosity of the medium as compared to the buffer solution. A rather strong dependence of the speed of bubble-propelled catalytic micromotors on the temperature was also re-confirmed by the study in Ref. [58]. Although it was not mentioned in Section 3, the duration of the self-propulsion at a constant speed could also become a problem when the speed of the catalytic micromotors is used as the analytical signal. For example, catalytic micromotors built with catalase were reported to have a constant speed only for about 2–3 min [52,58]. Such a short time-period characterized by self-propulsion at a constant speed might be a problem in the hands of untrained users (who might read the speed of the catalytic micromotors at too long times, and, thus, draw incorrect conclusions regarding the concentration of the analyte of interest). Catalytic micromotors characterized by a constant self-propulsion speed for long time periods (e.g., 5–10 min) are needed when such structures are to be used for reliable biosensing.
5. Sensing Analytes Which Are Not Involved at All in the Catalytic Process Propelling the Micromotors
Section 3 and Section 4 describe the way catalytic micromotors can be used to sense analytes which impact the catalytic process propelling the micromotors, and, thus, the motion of the micromotors (see also Figure 2A). However, catalytic micromotors can also be built to detect analytes which are not involved at all in these catalytic processes (see also Figure 2B). In such cases, the catalytic micromotors are used to enhance the analyte-proportional analytical signals in several ways:
- (i).
- By enhancing mass transport, and, thus, enhancing the probability of the biorecognition event to happen. Enhancing mass transport by the self-propulsion of catalytic micromotors comes with some advantages. For example, it does not require laboratory equipment (e.g., magnetic stirrers, shakers, vortex mixers, etc.), and, thus, it is suitable to be used both in specialized laboratories and outside specialized laboratories, in resource poor areas. Enhancing mass transport by the self-propulsion of catalytic micromotors can also be expected to eliminate some previously described inconsistencies [62] which characterize traditional ways of sample agitation. However, no studies have addressed this issue yet. No thorough comparison of mass transport enhancements by catalytic micromotors and by classic approaches was carried out. However, few papers do show that micromotors provide better results than classic stirring/agitation [63,64] (but without providing any explanation for the observed differences). Unlike classic ways to stir and mix samples, catalytic micromotors are also suitable to stir/mix very low volume samples (e.g., 10 µL of serum, saliva, or sweat placed on a glass microscope slide).
- (ii).
- By enhancing the local concentration of optical/electrochemical probes. For example, SiO2-coated Ag nanowires are not only excellent probes for surface-enhanced Raman spectroscopy (SERS) but also show positive phototaxis, that is, they self-propel towards the light source via photocatalytic processes. The latter ability can be used to pre-concentrate the probes and improve the sensitivity and the detection limit of SERS-based detection [65]. Catalytic micromotors were also made using magnetic materials, such as Ni [17,19,46] or Fe3O4 [64]. In turn, these facilitated the magnetic pre-concentration of the catalytic micromotors onto the surface of the electrode for the electrochemical quantification of the analyte (which they have collected during self-propulsion in the investigated sample) [46,64].
- (iii).
- By chemically transforming the targeted analyte. For example, Mg-based catalytic micromotors self-propel in aqueous solution while producing H2 and OH- ions, and the latter species can facilitate the electrochemical detection of diphenyl phthalate by converting this, electrochemically inactive, compound into electrochemically active phenol [49]. A similar concept was also applied for the detection of paraoxon (a cholinesterase inhibitor) [66]. OH- ions produced by catalytic micromotors facilitated also the detection of phenylenediamines by oxidizing these species to colored products [67].
The structure of the catalytic micromotors increases in complexity when they are used to detect analytes not directly involved in the catalytic process propelling the catalytic micromotors. Such micromotors must carry not only the catalyst that facilitates the self-propulsion but also the recognition elements (which bind selectively the targeted analytes) and the optical/electrochemical labels (which facilitate quantifying the extent of target binding). To substantiate this idea, Figure 7 schematically shows the steps involved in the making and the using of catalytic micromotors for the detection of immunoglobulin G (IgG) (see also Ref. [68] for additional details). The micromotor depicted in Figure 7 has a Pt inner layer, which facilitates self-propulsion by the decomposition of H2O2, and an IrO2 outer layer with a dual role: to carry antibodies for the selective recognition of the analyte of interest and to act as catalyst for the hydrogen evolution reaction during the detection stage. The sensing concept also needs magnetic particle-labeled secondary antibodies (see Figure 7B), which will facilitate the concentration of the micromotors onto the surface of the electrode used in the detection stage (see Figure 7C). There are more than ten main steps involved in the making and the using of the catalytic micromotors. Such a high number of steps makes achieving reproducible measurements very difficult. Important to note: instead of using motion as the analytical signal, catalytic micromotor sensors of this category rely on either electrochemical signals (as shown in Figure 7C) or optical signals (as shown in Figure 7D).
Figure 7.
Schematic representation of the procedure to build IrO2 on Pt microtube catalytic micromotors (A), the formation of antibody–antigen–antibody complexes on the surface of the catalytic micromotors (B), the electrochemical quantification of the analyte concentration via the hydrogen evolution reaction (C), and the detection of bacteria endotoxin with catalytic micromotors which change fluorescence in the presence of the bacteria endotoxin (D); (Obs.: The targeted analyte is not involved in the catalytic process facilitating self-propulsion. However, self-propulsion is enhancing the probability of the catalytic micromotors to bind analyte molecules found in the sample.) Figures reproduced with permission from Ref. [68] (panels (A–C)) and Ref. [69] (panel (D)).
Table 3 summarizes catalytic micromotors used for sensing species which are not directly involved in the catalytic processes of self-propulsion. In yet other words, the targeted analytes listed in Table 3 are neither fuel for the catalytic micromotors, nor inhibitors or activators of the catalytic processes facilitating self-propulsion.
Table 3.
Examples of micromotors which were used for sensing analytes which are not directly involved in the catalytic processes propelling the micromotors; (Used abbreviation: EDTA = ethylenediaminetetraacetic acid).
If one compares Table 3 with Table 1 and Table 2, it becomes clear that sensing with catalytic micromotors is dominated by concepts which are not using the parameters of the motion of catalytic micromotors as the analytical signal.
There are several other points one can make based on the information summarized in Table 3. Instead of using the motion of catalytic micromotors as the analytical signal, the sensing concepts listed in Table 3 deliver either optical signals (76% of the micromotors) or electrochemical signals (24% of the micromotors). As such, these sensing concepts carry the problems characterizing the optical and electrochemical detection principles. For example, photobleaching remains a major problem of concepts based on fluorescence. Interferences and drifts (e.g., due to electrode fouling) can complicate biosensing concepts based on electrochemical detection. The catalytic micromotors get a new role in the concepts listed in Table 3 (as compared to the concepts listed in Table 1 and Table 2): they are used to enhance the mass transport in the investigated sample. Interestingly, the analytical signals obtained with mass transport enhanced by the self-propulsion of catalytic micromotors were found sometimes larger (e.g., in Refs. [78,81]), sometimes equal, and sometimes smaller (e.g., in Ref. [82]) than the analytical signals obtained with classic ways for stirring and mixing liquid samples (e.g., magnetic stirring). A thorough comparison of catalytic micromotors with classic tools for stirring and mixing liquid samples was not yet carried out. However, one must keep in mind that stirring and mixing liquid samples with catalytic micromotors requires no additional laboratory equipment and that there are very few tools to carry out stirring and mixing in samples of only few microliters volume. Enhancing the mass transport in the investigated sample was most often done with catalytic micromotors ejecting O2 bubbles by the decomposition of H2O2 (and only few times with micromotors which generate H2 bubbles via the reaction of Mg and H2O). Self-propulsion based on the ejection of O2 bubbles generated in H2O2, while more robust than phoretic self-propulsion, is still characterized by weaknesses (some of which were already mentioned in previous sections and will not be repeated here). O2 bubbles are only generated at high H2O2 concentrations (0.8–7.5%) and high H2O2 concentrations can oxidize sample components and cause problems both in electrochemical detection (as H2O2 is oxidized and reduced at relatively low applied potentials) and in optical detection (e.g., H2O2 concentrations higher than 7% were found to quench the CdTe quantum dots-based fluorescence of some catalytic micromotors [70]). In addition, the chemical composition of the investigated sample was also found to impact the speed of O2 bubble ejection-based catalytic micromotors. Some organic species (e.g., dimethyl sulfoxide) can quench radicals involved in the decomposition of H2O2 while others (e.g., thiols, furfural, and ethanol) can irreversibly adsorb onto the catalyst with detrimental effects on its ability to decompose H2O2 [86,87]. It is currently not clear (as it was not studied) how much the speed of the self-propulsion can decrease/increase (due to the combined effects of viscosity, organic species, temperature, etc.) without affecting the analytical signal in the sensing concepts listed in Table 3.
One can also note that selectivity tests are sketchy, in the best case, as the number of samples analyzed (after calibration with standard solutions) is very low (e.g., 2–3) in most of the available studies. The fact that catalytic micromotors were not tested with a larger number of complex (i.e., “real world”) samples is most likely due to the complexity of making the catalytic micromotors and using them for sensing purposes, as well to the (prohibitively large for most of the laboratories) time and costs demanded by such extensive validation studies.
6. Conclusions
Proof-of-principle studies of detection of analytes by using catalytic micromotors have been reported for a large number of very different type of analytes: e.g., metal ions, low molecular weight biomolecules, biomacromolecules, viruses, gases, etc. The analytes detected with catalytic micromotors are of interest in various fields, such as biomedicine, environment protection and remediation, and food safety. Few of these analytes were detected as they could also act as fuel for the catalytic micromotors (see Section 3). Other analytes were detected because they could modulate (e.g., inhibit or activate) the catalytic processes behind the self-propulsion of catalytic micromotors (without being the actual fuel of the catalytic micromotors; see Section 4). Most of the analytes were detected based on optical or electrochemical methods enhanced by catalytic micromotors. The ability of self-propelling catalytic micromotors to stir and mix the investigated sample was very important in this latter case (see Section 5). This ability is critical when the investigated sample is a tiny liquid droplet that cannot be stirred and mixed with classic laboratory equipment. Real-Time PCR [21,72], electrochemical biosensors [19,58,64,68,69,81,82], optical biosensors [19,58,64,69,75,81,82], enzyme-linked immunosorbent assays [22,64], and the limulus amoebocyte lysate test [69,81,82] are among the analytical tools compared to catalytic micromotor sensors. The analytical performances (most often the detection limit, sometimes the accuracy) of catalytic micromotor sensors were found sometimes better [64,68,75,81,82], sometimes similar [21,22,72,75,82], and sometimes worse [19,58,69,75] than those of the classic counterparts. The outcome of such a comparison obviously depends very much on the analytical tools selected as reference points. The shorter analysis times they facilitate and the extremely low volumes of sample they need are still undeniable advantages of the catalytic micromotor sensors.
However, as discussed in this review, there remain, in our opinion, a lot of aspects to be improved in what concerns the fabrication and use of catalytic micromotors as sensors. Most of the catalytic micromotors are produced by putting together several different materials via complicated, multistep procedures. We are clearly far from being able to mass produce highly reproducible, catalytic micromotors. Important properties (e.g., the speed of self-propulsion) of the currently produced catalytic micromotors show inconveniently large dispersions. Moreover, numerous details of the sample (e.g., viscosity, temperature, ion content, concentration of thiols, etc.), rather than just the concentration of the analyte of interest, seem to impact the behavior of catalytic micromotors, and thus the result of the “measurement”, in seemingly uncontrolled, and not well understood, ways. Most studies considered only a small number of “real-world” samples (e.g., 2–3) and thus the reliability of the sensing concepts based on catalytic micromotors remains poorly demonstrated; moreover, the proof-of-concepts studies are only seldom followed-up by thorough comparisons with reference analytical methods.
Accordingly, the conclusion that emerges from the available studies is that the qualitative (rather than quantitative) analysis of small samples in resource poor environments is the most promising niche area for the catalytic micromotors in analytical chemistry.
Author Contributions
Writing—original draft preparation, M.N.P. and S.G.; Writing—review and editing, M.N.P. and S.G. All authors have read and agreed to the published version of the manuscript.
Funding
This research was funded by the Romanian Executive Unit for Higher Education, Research, Development and Innovation Funding through grants PN-III-P4-PCE-2021-1231 (contract no. PCE 21 from 26 May 2022) and ERA-Net EuroNanoMed (contract no. 135 from 9 March 2020).
Institutional Review Board Statement
Not applicable.
Informed Consent Statement
Not applicable.
Data Availability Statement
Not applicable.
Conflicts of Interest
The authors declare no conflict of interest.
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