$$\rightleftharpoonup{xx}$$
$$\longleftharp{xx}$$,
$$\longrightharp{xx}$$,
Electrocatalytic interruption mitigates edge effects by shifting the primary current generation mechanism from diffusion-limited (i.e., limited by the transport of a redox probe to the electrode) to kinetically limited (i.e., limited by a rapid, solution-phase reaction)20. This method is modular, meaning it allows a mix-and-match approach to choosing the electrode material, redox probe, and substrate, and this renders electrocatalytic interruption amenable to the detection of many nano- and bio-materials6,7,8,9,10,11,12,13,14,15,22. Implementing this technique on a 5.5 µm radius carbon-fiber electrode produced a 10-fold improvement in the precision associated with the electrochemical sizing of a model system (polystyrene beads) in a solution containing TEMPO as a redox probe and maltose as a substrate.
Following this protocol, the data sets required to validate this mechanism and its ability to restore analytical precision when sizing electro-inactive nanoparticles can be obtained. First, the cyclic voltammogram data collected in the absence of polystyrene beads showed a reversible redox event in control experiments involving TEMPO alone. From here, the addition of maltose resulted in an increase in the oxidative peak and a concurrent loss in the reductive peak as the oxidized TEMPO was regenerated by maltose. Second, the chronoamperograms collected under these conditions demonstrated that the steady-state currents at an oxidative potential were higher, consistent with the catalytic amplification observed in the cyclic voltammetry results. This step also suggests that the bulk chemical reaction is maintained by the electrode reaction; thus, any improvements over the control method will last over the measurement duration. However, this alone is insufficient for assessing any improvements to the measurement precision; to do so, chronoamperometry data must be collected in the presence of polystyrene beads.
To assess the sizing precision, chronoamperogram data were collected using 2 µm carboxylated polystyrene beads. Upon their addition, step-wise changes in the chronoamperogram current were observed as individual particles impacted and absorbed (Figure 2A control, Figure 2B electrocatalytic interruption). Each step-wise change in the steady-state current magnitude was converted to particle radii, and the data were visualized as histograms to compare the distribution from these electrochemical techniques to that of a gold standard technique, such as scanning electron microscopy (Figure 3). This comparison then allowed the characterization of precision metrics associated with each sizing approach.
Modeling was utilized to support these experimental observations. Specifically, fitting the cyclic voltammograms from before yielded parameters that characterized both the electrode reaction and the solution-phase chemical reaction (Figure 4). From the control solution, some sample parameters obtained were Efθ = 0.49 V, k0 = 0.02 cm·s-1, and ν = 10 mV·s-1 at T = 25° C. From the test solution, the kinetic parameters that limited current generation could be obtained; specifically, as Keq approaches infinity, kobs = 2,200 M-1·s-1. The numerical simulations could then use these values as the initial conditions for generating a concentration profile of the redox probe (Figure 5). In the absence of maltose, the resultant diffusion profile was radial, leading to heterogeneous material flux; specifically, more material diffused to the electrode at the edges. The introduction of maltose compressed the diffusion profile, producing, in turn, more homogeneous currents across the electrode surface.

Figure 1: Schematic of the experimental protocol. Polish the electrodes prior to each experimental run. Collect a baseline set of electrochemical measurements (cyclic voltammetry and chronoamperometry) in the absence of beads with and without implementing electrocatalytic interruption to observe the current enhancement with the addition of the substrate. Spike in the beads, and collect a second set of electrochemical measurements for the size determination of the impacting nanoparticles. Validate the mechanism of action using numerical simulations. Please click here to view a larger version of this figure.

Figure 2: Chronoamperograms collected using an 11 µm diameter carbon-fiber ultramicroelectrode demonstrating the improvement in measurement precision achieved using electrocatalytic interruption. Specifically, when measuring the current versus time in a solution of 1 mM TEMPO in the (A) absence (control) and (B) presence of 120 mM maltose (electrocatalytic interruption), the steps observed in the latter case were more homogeneous. Reprinted with permission from Chung et al.20. Please click here to view a larger version of this figure.

Figure 3: Precise electrochemical sizing data when using electrocatalytic interruption compared to the conventional, diffusion-limited electrochemical approach. To represent this data, prepare histograms comparing the size distributions determined using scanning electron microscopy (light grey) and electrochemistry (electrocatalytic interruption, pink; control, dark grey). Conventional nanoimpact studies, in which the current is limited by the mass transport of the mediator, produce artificially broad estimated size distributions (dark grey). In contrast, implementing electrocatalytic interruption leads to narrower, more precise size estimations (pink). Reprinted with permission from Chung et al.20. Please click here to view a larger version of this figure.

Figure 4: Modeling the electrode kinetics to characterize the new reaction scheme. Using cyclic voltammogram fitting software, extract the electrode reaction parameters from the experimental data. (A) Data with 1 mM TEMPO. (B) Data with 1 mM TEMPO plus 120 mM maltose. Reprinted with permission from Chung et al.20. Please click here to view a larger version of this figure.

Figure 5: Changes in material flux at the electrode surface upon introducing electrocatalytic interruption visualized by numerical simulations. (A) The addition of maltose compresses the diffusion layer in a concentration-dependent manner. (B) The addition of maltose depresses the heterogeneous flux at the electrode edges. Reprinted with permission from Chung et al.20. Please click here to view a larger version of this figure.