In current-blockade impact electrochemistry, insulating particles are detected amperometrically as they impinge upon a micro- or nanoelectrode via a decrease in the faradaic current caused by a redox mediator. A limit of the method is that analytes of a given size yield a broad distribution of response amplitudes due to the inhomogeneities of the mediator flux at the electrode surface. Here, we overcome this limitation by introducing microfabricated ring-shaped electrodes with a width that is significantly smaller than the size of the target particles. We show that the relative step size is somewhat larger and exhibits a narrower distribution than at a conventional ultramicroelectrode of equal diameter.
In current-blockade impact electrochemistry, insulating particles are detected amperometrically as they impinge upon a micro- or nanoelectrode via a decrease in the faradaic current caused by a redox mediator. A limit of the method is that analytes of a given size yield a broad distribution of response amplitudes due to the inhomogeneities of the mediator flux at the electrode surface. Here, we overcome this limitation by introducing microfabricated ring-shaped electrodes with a width that is significantly smaller than the size of the target particles. We show that the relative step size is somewhat larger and exhibits a narrower distribution than at a conventional ultramicroelectrode of equal diameter.
Particle-impact electrochemistry
is a set of techniques, in which
individual micro- and nanoscale entities are detected in real time
as they impinge upon a miniaturized electrode. Depending on the electroactivity
of the particles and of the electrode, particle collisions lead to
various types of stochastic, discrete signatures in amperometric measurements.
Information on the particles such as surface properties, catalytic
activity, size, and even shape can be inferred from these measurements,[1−12] also in optically opaque solutions.[13] Impact methods have also been used for detecting individual biomolecules[14−18] and have been suggested as candidate single-entity electrochemical
transducers for digital biosensing.[19]An early variant of particle-impact electrochemistry is current
blockade. Here, insulating particles are detected as a decrease in
an otherwise steady-state amperometric signal as they interfere with
the mass transport of a redox mediator to the electrode.[20] In addition to inert synthetic particles, this
method has been employed to detect bacteria,[21] vesicles,[22] viruses,[17] and biomolecules.[15] It has further
been employed as a tool for characterizing the size of biomacromolecules[15] and graphene oxide sheets.[23] A limitation of the method, however, arises because the
size of the steps in the measured current depends on the location
of the particle on the electrode.[24,25] This occurs
because the mediator flux is not uniform over the surface of a planar
electrode, as illustrated in Figure a. For a disk ultramicroelectrode (UME), for example,
the current density is highest near the rim of the electrode and smallest
at its center.[26] This inhomogeneity causes
two main problems in particle blockade measurements with disk-shaped
UMEs: (1) false-positive events introduce error in particle-counting
experiments[24,25] and (2) biases are introduced
in particle-sizing experiments that are based on the amplitude of
the current-blockade steps.[24,25]
Figure 1
Schematic representation
of disk and ring UMEs. (a) For the disk
UME, the region near the rim of the disk has the highest mediator
flux and correspondingly the highest current density. The current
density (given by eq ) is minimal at the center of the electrode, but with a large region
surrounding the center, where it is nearly constant. Because of the
variations in current density, particles landing near the center or
the edge of the disk lead to different signal sizes. (b) For the ring
UME, the mediator flux and the current density are uniform along the
circumference. Variations across the thickness of the ring do occur,
but on such a small length scale that they are averaged over in a
particle-impact experiment. This leads to consistent current steps.
Because migration usually dominates transport of the particles in
impact experiments, the particles are attracted to the ring and remain
confined in the cavity.
Schematic representation
of disk and ring UMEs. (a) For the disk
UME, the region near the rim of the disk has the highest mediator
flux and correspondingly the highest current density. The current
density (given by eq ) is minimal at the center of the electrode, but with a large region
surrounding the center, where it is nearly constant. Because of the
variations in current density, particles landing near the center or
the edge of the disk lead to different signal sizes. (b) For the ring
UME, the mediator flux and the current density are uniform along the
circumference. Variations across the thickness of the ring do occur,
but on such a small length scale that they are averaged over in a
particle-impact experiment. This leads to consistent current steps.
Because migration usually dominates transport of the particles in
impact experiments, the particles are attracted to the ring and remain
confined in the cavity.False-positive detection
events are the first consequence of the
inhomogeneous flux of redox mediators on disk UMEs. In most blockade
impact experiments, migration is the dominant mode of transport for
charged particles, while the flux of the inert redox mediator remains
diffusion-limited.[1] The disk edge exhibits
a higher flux density and, consequently, a stronger residual electric
field. Hence, charged particles tend to migrate toward the edge of
the UME. Furthermore, as a result of this electrophoretic
edge effect, particles that are adsorbed near the center
of the electrode subsequently migrate toward the edge. This dynamic
rearrangement of particles leads to unwanted steps that result in
overestimates during particle counting measurements.[24,25]The second issue is the uneven signal that is due to the mediator edge effect. Due to the non-uniform mediator flux,
the location where particles land on the surface can cause uneven
current step sizes, with particle collisions near the edge of the
disk leading to bigger steps than near the center. This occurs independently
of whether particles are transported primarily by migration or diffusion.
This issue complicates signal analysis in blockade impact measurements,
and in particular renders particle size measurements difficult. In
blockade impact, particle size (radius, rΔ) can be estimated from the current step magnitude
using , where iss is
the steady-state current, Δiss is
the current step magnitude, a is the radius of the
UME, and α is a numerical factor that depends on the electrode
geometry.[15] This expression, however, neglects
the variability in the step size introduced by the mediator edge effect.[25] Uneven current steps can also indirectly affect
particle-counting measurements if collisions near the disk center
lead to steps that are smaller than the background noise, while collisions
at the edge cause measurable steps. This limits the useable electrode-to-particle
size ratio.[27] Finally, a variable step
size is particularly problematic if a particular step size Δiss is used as the signature of a specific event
such as in biorecognition.[28]Because
the discrepancies in the signal size and frequency both
stem from the inhomogeneous flux of the redox mediator, solving this
issue can significantly improve the accuracy of blockade impact measurements.
Recently, Renault et al. demonstrated a way to circumvent non-uniform
flux by using a hemispherical electrode, for which the current density
is uniform over the surface of the electrode.[29] This uniformity stems from the spherical symmetry of this geometry,
at least under conditions, where surface conduction and electrokinetic
effects caused by the insulating shroud surrounding the electrode
can be neglected. In this work, the electrodes were realized using
liquid Hg. While it serves as an important proof of concept, this
system remains somewhat impractical for routine measurements due to
the additional fluid handling and safety considerations attached to
Hg.Here, we introduce an alternative electrode geometry to
overcome
the non-uniform flux of redox mediators in blockade impact electrochemistry.
The electrodes, which are fabricated using optical lithography, consist
of a ring that is thinner than the particles to be detected. The structure
is analogous to ring electrodes in some ring-disk electrode pairs
used for redox cycling and generator-collector experiments.[30,31] This approach avoids the problems caused by an inhomogeneous current
density. Particles colliding at any position along the circumference
of the ring encounter a similar environment. Furthermore, while the
mediator flux does vary across the width of the ring, the larger size
of the particles ensures that the measured signal includes contributions
from the entire distribution of fluxes (Figure b), largely eliminating positional effects.
In a migration-limited regime, particles remain confined to the contour
of the ring through the electric field and block a similar amount
of redox molecules. Furthermore, this geometry is fully compatible
with planar microfabrication methods, unlike a hemispherical geometry,
while also allowing impact measurements at current densities higher
than those encountered at disk UMEs of the same diameter. We show
experimentally that ring electrodes exhibit a narrower distribution
of step sizes and a higher relative size sensitivity when compared
to data for disk electrodes of the same diameter.
Experimental
Section
Chemicals and Instrumentation
In this study, we employed
1,1′-ferrocenedimethanol (Sigma-Aldrich, 372625) as the redox
mediator and KCl (Sigma-Aldrich, P9333) as the supporting electrolyte.
All the measurements were performed using 1 μm diameter (standard
deviation = 0.03 μm) polystyrene beads (Polysciences, 07310).
The zeta potential of the polystyrene beads was measured in working
solution (0.67 mM ferrocenedimethanol and 7.5 mM KCl) using a Zetasizer
Nano ZS (Malvern Panalytical). The 10 μm disk platinum UME was
purchased from BASi (BASi/MF-2005). The Pt disk was polished with
alumina slurry (1, 0.3, and 0.05 μm, Buehler, Lake Bluff, U.S.A).
Milli-Q water with 18.2 MΩ·cm–1 resistivity
(Milli-Q Advantage A10) was used for preparing all the solutions.
Device Fabrication
Ring and disk UMEs with different
diameter were fabricated on the same chips using a combination of
thin-film deposition, optical lithography, and etching procedures. Figure a represents the
fabrication process flow schematically; the steps described below
correspond to the numbered sub-panels in Figure a. The full process flow is also illustrated
in Figure S1.
Figure 2
(a) Schematic representation
of cross section at different steps
of the process flow for the fabrication of disk and ring UMEs: 1—wet
oxidation, 2—SiN deposition by PECVD, 3—sputtering of
Ti and Pt via T’COathy, 4—lithography (alignment and
exposure) and development of the photoresist, 5—etching Pt
and Ti layers via IBE and stripping of the photoresist, 6—SiN
deposition via PECVD, 7—lithography and development of the
photoresist, 8—etching SiN layer via RIE (exposing the disk
UMEs and external connections) and stripping of the photoresist, 9—lithography
and development of the photoresist, and 10—etching SiN/Pt–Ti/SiN
layers using a combination of RIE/IBE/RIE methods (exposing the ring
UMEs) and stripping of the photoresist. (b) Optical microscopy image
(top view, scale bar 1 mm) of the fabricated device. (c) Optical microscopy
image (top view, scale bar 100 μm) of the fabricated device
showing interconnects and electrodes of different sizes at the center.
(d) Scanning electron microscopy (SEM) image of a ring UME with diameter
of 10 μm and a thickness of 50 nm from a 45° viewing angle
(scale bar 1 μm). Pt appears as a bright ring.
(a) Schematic representation
of cross section at different steps
of the process flow for the fabrication of disk and ring UMEs: 1—wet
oxidation, 2—SiN deposition by PECVD, 3—sputtering of
Ti and Pt via T’COathy, 4—lithography (alignment and
exposure) and development of the photoresist, 5—etching Pt
and Ti layers via IBE and stripping of the photoresist, 6—SiN
deposition via PECVD, 7—lithography and development of the
photoresist, 8—etching SiN layer via RIE (exposing the disk
UMEs and external connections) and stripping of the photoresist, 9—lithography
and development of the photoresist, and 10—etching SiN/Pt–Ti/SiN
layers using a combination of RIE/IBE/RIE methods (exposing the ring
UMEs) and stripping of the photoresist. (b) Optical microscopy image
(top view, scale bar 1 mm) of the fabricated device. (c) Optical microscopy
image (top view, scale bar 100 μm) of the fabricated device
showing interconnects and electrodes of different sizes at the center.
(d) Scanning electron microscopy (SEM) image of a ring UME with diameter
of 10 μm and a thickness of 50 nm from a 45° viewing angle
(scale bar 1 μm). Pt appears as a bright ring.A one-side polished (OSP) silicon wafer (⟨100⟩,
boron-doped
p-type) with a thickness of 525 ± 25 μm was used as the
substrate. Wet oxidation of silicon was performed to grow a 500 nm
SiO2 layer (step 1). A 100 nm silicon nitride (SiN) layer
was then deposited via PECVD (step 2). In step 3, 5 nm titanium (Ti)
as the adhesion layer and 50 nm platinum (Pt) were sputtered using
an ion-beam system (home-built T’COathy system, MESA + NanoLab,
the Netherlands). Standard optical lithography was then performed
to define the geometry of the metal electrodes as well as connecting
wires and pads for external connections (step 4). After developing
the resist, in step 5, the 50/5 nm Pt/Ti layers were etched via ion
beam etching (IBE, Oxfordi300Plus), and the photoresist was stripped
with O2 plasma (TePla300, PAV TePla AG, Germany). In step
6, the second layer of SiN (100 nm) was deposited on the surface via
PECVD. In step 7, standard lithography was again performed to expose
disk electrodes and mm-scale connections to the device. Then, the
exposed SiN layer was etched via reactive ion etching (RIE) with CHF3/O2 plasma (home-built TEtske system, MESA+ NanoLab,
the Netherlands), and the photoresist was stripped with TePla300 (step
8). In order to create the ring electrodes, standard lithography was
again performed as per the above (step 9). The exposed circular areas
with diameters of 2.5, 5, and 10 μm were etched using a combination
of RIE/IBE/RIE to etch the SiN/Pt/SiN layers, respectively (step 10),
and the photoresist was stripped with O2 plasma. Due to
the slow etch rate of the RIE for Pt, IBE was used for etching this
layer. Complete etching of the bottom layer of SiN was monitored using
optical microscopy; exposure of SiO2 in the 10 μm
diameter wells led to a color change. The wafer was coated with photoresist
before dicing to prevent contamination during dicing.
Electrochemical
Measurements
The measurements were
performed using a two-electrode configuration in a custom Faraday
cage. No auxiliary electrode was required as the current levels remained
on the order of ∼1 nA or smaller. A constant potential of +0.35
V was applied to a microfabricated Pt ring or a commercial Pt disk
(BASi/MF-2005) working electrode with respect to the Pt pseudoreference
electrode wire (0.20 mm diameter, ∼4 mm length exposed to solution),
corresponding to an oxidizing overpotential. Data for the commercial
UME are shown here to facilitate comparison to other works, but the
on-chip disk UMEs yielded equivalent results. A transimpedance amplifier
(Femto, DDPCA-300, GmbH, Berlin, Germany) and a homemade Labview (v2013)
program were used to monitor the current. The measurements were performed
using 1 μm diameter polystyrene particles with a density of
4.55 × 1010 particles/mL (stock solution). The particle
solution was diluted 500 times in 0.67 mM ferrocenedimethanol as the
redox mediator (prepared in Milli-Q water) as the working solution
for the measurements. We further employed KCl as the supporting electrolyte
with a concentration of 7.5 mM in all the measurements. The UME was
polished mechanically in a figure-eight motion with alumina particles
with sizes of 1.0, 0.3, and 0.05 μm polish, rinsing the electrode
between the different polishing steps. For the microfabricated devices,
individual diced chips were successively cleaned with acetone, Milli-Q
water, and isopropyl alcohol and sonication for 5 min for each step
so as to remove a protective photoresist protective layer introduced
for dicing. The chips were placed in a homemade stage including a
custom socket for making connections [36-pin Land Grid Array (LGA)
package, 0.70 mm pitch, Interconnect Devices (IDI)]. A polydimethylsiloxane
cylinder was used as the cell, and the pseudoreference electrode was
inserted through the top opening. The experimental geometry is illustrated
in Figure S2.
Numerical Simulations
In order to obtain a more quantitative
assessment of the current density on disk UMEs, finite-element calculations
of the diffusive mass transport of the redox mediator to three-dimensional
models of the electrode were performed. These finite-element numerical
simulations were performed with COMSOL Multiphysics 5.3a (Supporting Information). The step size was calculated
by subtraction of the steady-state current with and without the particle
on the surface.
Analysis of Experimental Current Steps
Due to the dependency
of the step size on the baseline current, the current step sizes (Δiss) were normalized to the steady-state current
(iss) immediately before each step, and
the Δiss/iss ratio was used to compare the step sizes in the two geometries.
Several measurements were performed to generate sufficient numbers
of steps for the statistical analysis. The total numbers of steps
were 476 for both the ring and disk UMEs. In order to limit the influence
of previously landed particles on the step size, a limited number
of collisions (at most 15 collisions from each measurement) were used
in the analysis. Using fewer collisions per experiment did not modify
the shape of the histograms apart from introducing more statistical
noise (Supporting Information). Due to
the decrease in the steady-state current, which is particularly pronounced
in the first seconds of the measurements, the steps were counted from
the second step to step number 16. The step size analysis was performed
using a custom script. First, the amperometric measurements were filtered
using a Savitzky–Golay filter to remove the high-frequency
noise. Each smoothed curve was then differentiated, and the location
of the steps was identified as sharp spikes in the resulting curve
(see the Supporting Information for details).
Results and Discussion
Our strategy for obtaining consistent
signals in current blockade
measurements is to create a ring electrode that is smaller in width
than the target particles to be detected, so that each particle-impact
event is geometrically equivalent regardless of where it occurs along
the circumference of the electrode. For micron-sized particles or
smaller, this implies nanoscale ring widths. While electron-beam lithography
is a good approach for the fabrication of planar electrodes with such
dimensions, it is not widely available and does not lend itself well
to large-scale production. In this report, we instead focus on standard,
widely available optical lithography techniques. To control the width,
we rely on the ability to control the deposition of thin films very
accurately. As a consequence of this, the ring electrode is embedded
in the wall of a shallow cavity rather than being fully planar. The
thickness of the ring is determined by the amount of metal deposited.
Although the fabricated device in this report could be used for analyzing
smaller particles, 1 μm particles were employed to be comparable
with the results of a conventional 10 μm disk UME experiment.
As illustrated schematically in Figure b, the particles are bigger than the height of the
SiN/Pt/SiN well. As a consequence, there is no direct contact between
the particle and the electrode surface, and the landed particles are
confined in the corner of the ring by the electric field.We
first present measurements on disk electrodes and analyze the
step size distribution in order to provide a baseline against which
the ring electrodes can be compared.
Disk UME Measurements
The diffusion-limited current
to a shrouded disk electrode is given by[26]Here, n is the number of
electrons, F is the Faraday constant, D is the diffusion coefficient of the redox species at concentration C, and a is the radius of the disk. A diffusion-limited
steady-state current of ≈850 pA was obtained experimentally
(Figure a), which
is in good agreement with the calculated value using eq (Itheoretical = 860 pA, D = 6.7 × 10–10 m2·s–1).
Figure 3
(a) Current–time
response of blockade impact measurement
with 10 μm disk UME, and 1 μm negatively charged particles
in 0.67 mM ferrocenedimethanol solution exhibits uneven current steps
with a range from ≈1 to 4 pA. (b) Histogram of the step sizes
for 476 current steps obtained in different measurements. The red
dashed curve represents the distribution obtained from eq with no fitting parameter. (c)
Chronoamperograms and CV of the measurements with the fabricated recessed
ring electrodes with 10 μm diameter and 50 nm thickness. (d)
Histogram of the step sizes for the 10 μm ring. The x-axes in (b,d) show the step size per mille (‰)
on a logarithmic scale (the data are also shown on a linear scale
in the Supporting Information). The step
size is normalized by the current immediately before each step. This
facilitates comparison with previous reports with different geometries
and measurements at different redox mediator concentrations.[29]
(a) Current–time
response of blockade impact measurement
with 10 μm disk UME, and 1 μm negatively charged particles
in 0.67 mM ferrocenedimethanol solution exhibits uneven current steps
with a range from ≈1 to 4 pA. (b) Histogram of the step sizes
for 476 current steps obtained in different measurements. The red
dashed curve represents the distribution obtained from eq with no fitting parameter. (c)
Chronoamperograms and CV of the measurements with the fabricated recessed
ring electrodes with 10 μm diameter and 50 nm thickness. (d)
Histogram of the step sizes for the 10 μm ring. The x-axes in (b,d) show the step size per mille (‰)
on a logarithmic scale (the data are also shown on a linear scale
in the Supporting Information). The step
size is normalized by the current immediately before each step. This
facilitates comparison with previous reports with different geometries
and measurements at different redox mediator concentrations.[29]For the negatively charged
1 μm particles, the supporting
electrolyte concentration employed here results in migration-limited
transport. This is in contrast to transport of the redox mediator,
which is diffusion-limited. This regime of transport was chosen to
ensure multiple discrete events per measurement over a practical time
scale. However, the supporting electrolyte ratio was sufficiently
high (>10) to suppress electroosmotic flows (EOF). This avoided
the
possibility that EOF could repel the colliding particles from the
electrode along the surface, which would lead to current spikes instead
of well-defined steps and would complicate interpretation.[32,33] This regime enables measurement of particles at ultralow concentrations,
decreasing the probability of particle adsorption on UME surfaces
before starting the measurements and the probability of particles
cocollision during the measurements.As can be seen in the raw
data of Figure a,
the current–time response of blockade
impact of 1 μm particles on a 10 μm disk UME exhibits
steps with uneven sizes with a range from approximately 1–4
pA. A histogram of the normalized magnitude of the steps is shown
in Figure b, illustrating
the broad distribution of step sizes in measurements with disk UMEs.
This has previously been explained as resulting from the inhomogeneous
current distribution at the surface (mediator edge effect).[20,24,25,29] This reasoning can be further formalized as follows. We define the
area of the electrode with a radius between r and r + dr, where dr is an
infinitesimal increment, as g(r)dr = 2πr dr. We similarly define the distribution of current
step sizes, gΔ(Δi)d(Δi), as the relative
number of sites on the electrode, where the step size falls in the
range Δi to Δi + d(Δi). Δi is a function of r because of the non-uniform mediator flux density. Equating g(r)dr = gΔ(Δi)d(Δi) yieldsThe probability
that a particular step has an amplitude Δi is
proportional to gΔ(Δi), because this dictates
the number of sites that yield this value of Δi, times the particle flux to that region. Noting that the mediator
current density j(r) at a disk electrode
as a function of radial position r has the form[34]and that
the migrational transport of particles
resulting from the residual ohmic electric field approximates the
same form, we have for the expected probability density of step sizesHere, B is a normalization
factor independent of r. In this simple model P(Δi) = 0 for r > a because there is no electric field driving the particles
to the insulating shroud; however, note that this simplification would
need to be lifted for situations, where diffusion contributes substantially
to particle mass transport.In order to evaluate eq for P(Δi), it is
necessary to have an expression for the dependence of the step size
Δi(r) on r. We evaluated this function using finite-element methods, as detailed
further in the Supporting Information.
The final predicted distribution, which does not include any free
parameter, is shown in Figure b. It exhibits two peaks. The peak at high step sizes corresponds
to particles landing near the edge; although this corresponds to a
small area, the collision density is high due to the stronger electric
field caused by the higher diffusive flux of redox mediator in this
region. The peak at low step sizes corresponds to collisions in the
central area of the disk with a larger area, but a lower current density
and electric field. While there is good agreement between the predicted
and measured range of current step sizes, the sharp peaks in the distribution
are not observed in the experiment. We attribute this additional broadening
to elements missing in the model including residual EOFs and the influence
of the finite particle size on migration in a non-uniform electric
field.
Ring UME Measurements
The geometry of the microfabricated
ring UMEs is shown in Figure . The ring electrodes were positioned in a shallow cylindrical
cavity with the electrode located on the side wall of the cavity.
The current to a thin planar ring (in the limit, where the width of
the ring Δ is much smaller than the ring radius ρ, Δ
≪ ρ) isWhile our geometry is more
complex,
this expression serves as a first approximation to estimate the current
levels that can be expected. The ratio of this current and of that
at a disk with the same radius (a = ρ) is Ilim,ring/Ilim,disk ≈ π2/2ln(32ρ/Δ). The slow inverse
logarithmic dependence of this ratio on the ring width, Δ, ensures
that even a thin ring can exhibit total currents of the same order
of magnitude as a disk UME of the corresponding diameter. In particular, eq predicts a ratio Ilim,ring/Ilim,disk ≈ 0.6 for our 10 μm diameter devices, which is remarkable
considering that the electrode area is a factor ≈50 times smaller
for the ring.The measurements with ring UMEs were performed
under the same conditions
as the disk measurements. The voltammogram of the fabricated 10 μm
diameter and 50 nm thick ring UME exhibits a typical sigmoidal shape
for diffusion-limited transport (inset, Figure c). A limiting current of ≈500 pA
was obtained. This corresponds to Ilim,ring/Ilim,disk = 0.59, in good agreement
with the theoretical estimate.Figure c shows
the amperometric response of a 10 μm diameter ring UME during
a current blockade measurement. Qualitatively, the response exhibits
relatively uniform step sizes. The frequency of collisions is comparable
to that for the disk electrode, consistent with the similar magnitude
of the current. Figure d shows the corresponding histogram of step sizes. The ring UME results
in a single, relatively narrow, peak representing uniform current
step sizes. This confirms the expectation of a more uniform current
density along the perimeter of the ring, in such a way that collision
of the particles anywhere on the ring blocks a similar amount of redox
mediator.More quantitatively, the standard deviations of the
step size for
the disk electrode (blue histogram) and ring electrode (red histogram)
are 0.25 and 0.13, respectively. In addition to the uniformity of
the signals, ring UMEs exhibit larger relative step sizes. These two
observations translate into a higher relative step size sensitivity
for rings under identical conditions.The histogram in Figure d nevertheless exhibits
a significant width. One might try
to explain this broad histogram as resulting from particles landing
close to each other after multiple collisions. If this were the case,
analyzing a lower number of steps per measurement should result in
a narrower distribution. However, the histogram shape and standard
deviation of the step size remain nearly unchanged in the ring UME
when analyzing the first 10, 7, or 5 steps of the same measurements
(Figure S5), ruling out this mechanism.The breadth of the histograms could also be due to non-idealities
in the experiment. One possibility is material redeposition in the
inner wall of the cavity in the last etching steps leading to a non-uniform
metal thickness. This non-uniformity can be improved in the future
by implementing alternative approaches for etching the SiN/Pt/SiN
stack. Material redeposition as well as an uneven etch depth inside
the ring may also lead to different particle heights when adsorbing
inside the ring. This can be mitigated in the future by etching deeper
so that the particles adsorb onto the electrode ring itself without
touching the bottom of the cavity. Another potential issue is adsorption
of the particles at random locations because no particular measures
were taken to protect against it. A final possibility is that the
assumption that all particles get jammed at the inner edge of the
cavity due to electrophoretic forces, as in Figure b, is oversimplified. Due to the nanoscopic
height of the ring electrodes, the electric field gradients created
are much larger than at conventional UMEs. This may lead to additional
effects such as dielectric forces, or electroosmosis that can normally
be ignored at the salt concentrations employed here. We envision that
particles may get trapped on the surface surrounding the cylindrical
cavity due to this complex balance of forces. Increasing the height
of the top and bottom layers of SiN or employing smaller particles
in a device with a thinner Pt layer can diminish this effect. Finally,
a true planar ring geometry could be implemented, at the cost of requiring
more sophisticated microfabrication equipment.
Conclusions and
Outlook
Here, we explored the use of ring electrodes with
a nanoscale width
as an alternative tool for detecting insulating particles via current-blockade
impact electrochemistry. We argued that the broad distribution of
step sizes for a disk can be explained semiquantitatively by a simple
model taking into account the non-uniform current distribution over
the surface of the electrode together with the resulting non-uniform
migrational flux of particles. In order to diminish the edge effect,
we designed and fabricated a ring geometry based on a thin strip electrode
sandwiched between insulating materials. The current-blockade impact
measurements using ring UMEs showed larger and more uniform relative
step sizes compared to a disk with the same diameter. In particular,
the distribution of step sizes for the ring UME is narrow enough to
reliably identify the simultaneous collision of two particles as a
double-sized step. Also, the occurrence of a single-step size distribution
should allow accurate particle size determination. This geometry further
addresses the particle displacement problem that leads to false collision
events. The step size uniformity can be further improved by fabricating
devices with more optimized geometries. The use of these ring UMEs
is not limited to current blockade: the fabrication process is relatively
straightforward and can be applied to different materials, such that
the advantages of ring UMEs can also be exploited in other impact
electrochemistry methods.
Authors: Jeffrey E Dick; Adam T Hilterbrand; Aliaksei Boika; Jason W Upton; Allen J Bard Journal: Proc Natl Acad Sci U S A Date: 2015-04-13 Impact factor: 11.205
Authors: Donald A Robinson; Aditya M Kondajji; Alma D Castañeda; Radhika Dasari; Richard M Crooks; Keith J Stevenson Journal: J Phys Chem Lett Date: 2016-06-21 Impact factor: 6.475
Authors: Jeffrey E Dick; Adam T Hilterbrand; Lauren M Strawsine; Jason W Upton; Allen J Bard Journal: Proc Natl Acad Sci U S A Date: 2016-05-23 Impact factor: 11.205