Sofia Arshavsky Graham1,2, Evgeniy Boyko3, Rachel Salama1, Ester Segal1,4. 1. Department of Biotechnology and Food Engineering, Technion-Israel Institute of Technology, Haifa 3200003, Israel. 2. Institute of Technical Chemistry, Leibniz Universität Hannover, Callinstr. 5, Hanover 30167, Germany. 3. Department of Mechanical Engineering, Technion-Israel Institute of Technology, Haifa 3200003, Israel. 4. The Russell Berrie Nanotechnology Institute, Technion-Israel Institute of Technology, Haifa 3200003, Israel.
Abstract
Porous silicon (PSi) thin films have been widely studied for biosensing applications, enabling label-free optical detection of numerous targets. The large surface area of these biosensors has been commonly recognized as one of the main advantages of the PSi nanostructure. However, in practice, without application of signal amplification strategies, PSi-based biosensors suffer from limited sensitivity, compared to planar counterparts. Using a theoretical model, which describes the complex mass transport phenomena and reaction kinetics in these porous nanomaterials, we reveal that the interrelated effect of bulk and hindered diffusion is the main limiting factor of PSi-based biosensors. Thus, without significantly accelerating the mass transport to and within the nanostructure, the target capture performance of these biosensors would be comparable, regardless of the nature of the capture probe-target pair. We use our model to investigate the effect of various structural and biosensor characteristics on the capture performance of such biosensors and suggest rules of thumb for their optimization.
Porous silicon (PSi) thin films have been widely studied for biosensing applications, enabling label-free optical detection of numerous targets. The large surface area of these biosensors has been commonly recognized as one of the main advantages of the PSi nanostructure. However, in practice, without application of signal amplification strategies, PSi-based biosensors suffer from limited sensitivity, compared to planar counterparts. Using a theoretical model, which describes the complex mass transport phenomena and reaction kinetics in these porous nanomaterials, we reveal that the interrelated effect of bulk and hindered diffusion is the main limiting factor of PSi-based biosensors. Thus, without significantly accelerating the mass transport to and within the nanostructure, the target capture performance of these biosensors would be comparable, regardless of the nature of the capture probe-target pair. We use our model to investigate the effect of various structural and biosensor characteristics on the capture performance of such biosensors and suggest rules of thumb for their optimization.
Biosensors
that monitor the
binding between a target molecule and a capture probe, by various
transducing methods and surface-based detection, in which the capture
probes are immobilized on the transducing surface, are among the most
widespread bioanalytical tools.[1−5] The performance of planar biosensors based on surface capture is
governed by the complex interplay between transport phenomena and
reaction kinetics, as modeled by Squires et al.(6) As such, numerous studies have been directed
to optimize these systems and elucidate their limiting factors.[7−14]Porous silicon (PSi) has been widely studied as an optical
transducing
surface in various biosensing platforms, presenting low cost fabrication,
chemically active surface, and unique optical properties.[15,16] Specifically, employing interferometric Fourier transform spectroscopy
(RIFTS) as the transduction mechanism enables real-time and label-free
target detection.[17−20] In this method, a series of Fabry-Pérot interference fringes
are produced from incident white light reflections from the top and
bottom interfaces of a porous thin film, and the fringe pattern depends
on the thickness and averaged refractive index of the porous layer.The porous nanostructure of PSi increases the surface area dramatically,
which allows the immobilization of a greater amount of capture probe
molecules compared to planar devices and potentially increases the
detection sensitivity by orders of magnitude.[16,21−25] Nevertheless, common detection thresholds in such systems revealed
an inferior performance, with micromolar detection limits for protein
and DNA targets in direct and label-free optical detection.[15,22,25−29] Therefore, many have focused on developing assays
for improving the sensitivity and performance of such systems,[15,26,27,29−31] while others investigated the limiting characteristics
of the platform and suggested solutions for overcoming these issues.[28,32−34] The latter includes mass transfer limitations, which
are affected by the nanostructure characteristics such as pore size,
height, porosity, surface area, and roughness.[32−40] For example, studies on the impact of the pore size on the binding
efficiency have been conducted,[39,41] and a critical correlation
between the molecule size and the pore diameter has been suggested
to allow effective infiltration into the porous layer, in which the
molecule must be at least five times smaller than the pore opening.[33] To overcome mass transport limitations, flow-through
platforms have been developed.[28,42] Moreover, accurate
quantitative determination of molecular binding kinetics was performed
by analyzing dilute analyte solution at short binding times, avoiding
capture probe saturation with the analyte.[43] The many parameters affecting the performance of PSi biosensors
challenge the experimental characterization of each factor. Thus,
deriving theoretical models to describe the effect of each of the
parameters is a facile way to study these complex systems.In
mesoporous systems, as the size of the pore approaches that
of the solute, a deviation from the diffusion kinetics predicted by
Fick’s law is observed, leading to an overestimation of the
solute flux.[44−46] The diffusion within the porous nanostructure is
hindered by steric and hydrodynamic interactions between the diffusing
solute, the pore wall, and the immobilized molecules and receptors
on the pore wall.[44,47−50] The structural properties of
the porous nanostructure, such as the pore diameter and porous layer
thickness, have also a tremendous effect, as the deviation from the
bulk diffusion coefficient is more pronounced for smaller pores and
a thicker layer.[51] The motion of the diffusing
molecule is also highly dependent on structural defects, as revealed
by single-molecule diffusion analysis in mesoporous silica.[52,53] Molecule transport and adsorption in porous materials have been
investigated, and models describing the hindered diffusion effect
have been empirically derived.[46,54] Nevertheless, the spatial
and time-resolved change in the diffusivity coefficient upon the filling
of the pore has been often neglected to simplify the solution of the
mass balances.[55−57]Further simplification of the mass transfer
studies in porous biosensors
has approximated the porous layer as a perfect collector, given the
large capacity of binding sites within the porous layer. Thus, the
entry into the pores has been concluded as the rate-limiting step,
while the hindered diffusion effect has been neglected.[28,58,59] Such modeling and analysis were
derived for protein adsorption on a porous anodic aluminum oxide nanostructure[58] and for PSi-based optical biosensors.[28,59] Nevertheless, for evaluation of the effect of mass transfer or reaction
kinetics in PSi-based biosensors, the system cannot be assumed as
a planar surface, and all transport phenomena and reaction between
the target and the immobilized probes should be considered.In this work, we aim to determine the effect of each of the mass
transport phenomena and reaction kinetics in PSi-based optical biosensors. In contrast to previous studies,
we develop a model which captures the complex mass transfer processes
in porous materials, including bulk diffusion, hindered diffusion,
and capture probe–target binding kinetics. The model is solved
numerically using parameters which are characteristic of typical PSi
biosensors. Specifically, we compare our model results to biosensing
experiments of several PSi-based aptasensors for proteins targets,
as well as to the common simplified “planar” model,
which neglects the hindered diffusion within the porous layer. Importantly,
we determine the limiting transport phenomena of PSi-based biosensors
and the dependency of the target binding rate on various biosensor
characteristics and conclude with directions for proper optimization
of such biosensors.
Materials and Methods
Materials
Heavily doped p-type Si wafers (⟨100⟩-oriented,
0.90–1.00 mΩ·cm resistivity) were purchased from
Sil’tronix Silicon Technologies (France). Aqueous HF (48%),
(3-aminopropyl)triethoxysilane (APTES), ethyldiisopropylamine (DIEA),
succinic acid, succinic anhydride, N-(3-dimethylaminopropyl)-N′-ethylcarbodiimide hydrochloride (EDC), N-hydroxysuccinimide (NHS), glutaraldehyde 25% solution
(GA), ethanolamine, acetonitrile (ACN), dimethyl sulfoxide (DMSO),
sodium cyanoborohydride, sodium dodecyl sulfate (SDS), N-succinimidyl 3-(2-pyridyldithio)propionate (SPDP), dl-dithiothreitol
(DTT), isopropyl alcohol (IPA), morpholinoethanesulfonic acid (MES),
MES sodium salt, Tris base, and all buffer salts were purchased from
Merck (Israel). Ethanol absolute was supplied by Bio-Lab ltd (Israel).
All solutions were prepared with Milli-Q water (ddH2O,
18.2 MΩ·cm). The anti-AGR2 aptamer sequence (5′-TCT-CGG-ACG-CGT-GTG-GTC-GGG-TGG-GAG-TTG-TGG-GGG-GGG-GTG-GGA-GGG-TT-3′)
was obtained from Wu et al.(60) The anti-his tag aptamer 6H7 sequence (5′-GCT ATG GGT GGT
CTG GTT GGG ATT GGC CCC GGG AGC TGG C-3′) was taken from U.S.
patent 7329742.[61] These aptamers were purchased
with a 5′-amino modification from Integrated DNA Technologies
(USA). The anti-protein A aptamer, selected by Stoltenburg et al.,[62] was used in the truncated
form PA#2/8[S1-58]: 5′-ATA CCA GCT TAT TCA ATT AGC AAC ATG
AGG GGG ATA GAG GGG GTG GGT TCT CTC GGC T-3′ and purchased
with 3′-amino-C6 modification. AGR2 protein was purchased from
MyBioSource Inc (USA). The mouse anti-his monoclonal antibody was
obtained from Enco (Israel). Streptavidin, biotinylated protein A,
and recombinant protein A from human serum were purchased from Merck
(Israel). 6xhis tyrosinase from Bacillus megatherium (recombinant,
expressed in Escherichia coli) was
generously supplied by Prof. Ayelet Fishman, Technion. His-tagged
AbnA-D2 (from Geobacillus stearothermophilus T-6, expressed in E. coli) (D2) was
generously supplied by Prof. Yuval Shoham, Technion. Phosphate-buffered
saline (PBS, 10 mM) was composed of 137 mM NaCl, 2.7 mM KCl, 10 mM
Na2HPO4, and 2 mM KH2PO4 (pH 7.5). AGR2 selection buffer was composed of 137 mM NaCl, 20
mM KCl, 10 mM Na2HPO4, and 2 mM KH2PO4 (pH 7.4). 6H7 selection buffer was composed of 50
mM K2HPO4 and 150 mM NaCl, pH 7.4, and elution
buffer was composed of 50 mM K2HPO4, 150 mM
NaCl, and 1 M Imidazole (pH 7.4). Protein A aptamer selection buffer
was composed of 20 mM Tris base, 100 mM NaCl, 5 mM KCl, 10 mM MgCl2, and 1 mM CaCl2. MES buffer (0.5 M) was prepared
from 0.27 M MES and 0.23 M MES sodium salt (pH 6.1), and Tris buffer
was composed of 50 mM Tris base (pH 7.4).
Construction of PSi-Based
Biosensors
The studied biosensors
include several PSi-based aptasensors and a representative immunosensor,
as detailed in Table . All biosensors employed a similar PSi nanostructure as the optical
transducer, and capture probe molecules (aptamer or antibody) were
immobilized onto the surface.
Table 1
Properties of the
Studied Capture
Probe and Target Protein Pairs and Comparison of the Theoretical and
Fitted KD Values
aptamer/antibody
target
molecular weight (kDa)
literature KD
fitted KD (μM)
anti-his tag aptamer
D2
60
∼4.6 μM[63]
29 ± 8 (R2 = 0.9551)
anti-his tag aptamer
tyrosinase
35
∼4.6 μM[63]
31 ± 7 (R2 = 0.9731)
anti-his tag antibody
tyrosinase
35
∼10 nM[64]
24 ± 5 (R2 = 0.9420)
anti-AGR2 aptamer
AGR2
22
∼13 nM[60]
21 ± 1 (R2 = 0.9951)
anti-protein A aptamer
protein A
45
∼0.522 μM[62]
14 ± 1 (R2 = 0.9177)
PSi Fabrication
PSi Fabry-Pérot
thin films are
fabricated from highly doped p-type crystalline Si wafers, with a
typical resistivity of 0.90–1.00 mΩ·cm, using a
two-step anodic electrochemical etching process. A detailed description
of the etching setup can be found elsewhere.[18] First, a sacrificial layer is etched at a constant current density
of 300 mA cm–2 for 30 s for the anti-AGR2 system
or 375 mA cm–2 for 30 s for the other systems, in
a 3:1 (v/v) solution of aqueous HF (48%) and ethanol, respectively.
The obtained porous layer is removed by introduction of 0.1 M NaOH,
followed by exposure to a solution of 1:3:1 (v/v) HF, ethanol, and
ddH2O, respectively. Next, a second etching is performed,
under the same etching conditions as mentioned above. After each step,
the silicon surface is thoroughly rinsed with ethanol and dried under
a nitrogen stream. Subsequently, the freshly etched PSi is thermally
oxidized in a tube furnace (Thermo Scientific, Lindberg/Blue M 1200
°C Split-Hinge, USA) at 800 °C for 1 h in ambient air to
create a chemically stable and hydrophilic oxidized PSi scaffold.[65]
Aptamer Immobilization
Amino-terminated
aptamers are
conjugated to the oxidized PSi films by carbodiimide coupling chemistry.
The first two steps of the chemistry, amino-silanization and carboxylation,
slightly differ in solvents and materials for each sensing system.
For anti-AGR2 aptamer immobilization, the oxidized PSi film is amino-silanized
by incubation in 1% v/v APTES and 1% v/v DIEA in ddH2O
solution for 1 h, followed by washing with ddH2O and ethanol
and drying under a nitrogen stream. Subsequently, the amino-activated
PSi samples are annealed at 100 °C for 15 min. Next, carboxylation
is achieved by incubation in a solution of succinic anhydride (10
mg mL–1) and 2% v/v DIEA in ACN for 3 h, followed
by extensive rinsing with ACN and ddH2O and drying under
a nitrogen stream.The anti-his tag aptamer, 6H7, and the anti-protein
A aptamer are immobilized by the method described by Urmann et al.(66,67) Briefly, the oxidized PSi films
are reacted with a solution of 42 mM APTES in toluene for 1 h, followed
by a thorough rinsing with toluene, ethanol, and acetone and drying
under a nitrogen stream. A similar annealing step is then performed,
as described above. The APTES-modified surface is then incubated in
a solution of 100 mg of succinic acid in 4.7 mL of DMSO and 300 μL
of 0.1 M NaHCO3 (pH 9.4) for 30 min, followed by washing
with DMSO and ddH2O and drying under a stream of nitrogen.Subsequently, for both systems, the carboxylated samples are reacted
with EDC (10 mg mL–1) in the corresponding selection
buffer for 1 h, followed by introduction of 50 μM anti-AGR2
aptamer or 75 μM anti-his tag or anti-protein A aptamers in
selection buffer and incubation for 1 h. The samples are then washed
with Tris buffer to deactivate the remaining reactive EDC groups on
the surface. Finally, the aptamer-functionalized PSi is exposed to
boiling ddH2O for 2 min and gently dried under a nitrogen
stream to unfold any secondary structures of the aptamer prior to
further use.
Antibody Immobilization
The oxidized
PSi surface is
first amino-silanized in 1% v/v APTES and 1% v/v DIEA in ddH2O solution for 1 h, followed by washing with ddH2O and
ethanol and drying under a nitrogen stream. Subsequently, the surface
is exposed to 2% aqueous GA solution for 30 min, washed with ddH2O, and dried under a nitrogen stream, followed by incubation
with 50 mM sodium cyanoborohydride in HEPES for 30 min, in order to
stabilize the Schiff base formed during reaction of the aldehyde groups
with the amine groups.[68] Next, the surface
is washed with HEPES, and streptavidin (100 μL; 100 μg
mL–1 in PBS) is applied and incubated for 1 h. The
surface is washed with PBS and stabilized again with sodium cyanoborohydride.
Next, a blocking step with 0.3 M ethanolamine in BBS buffer (0.15
M borate buffered saline, pH 9.0) is carried out for 30 min, followed
by washing with BBS and PBS buffers. Finally, the surface is reacted
with biotinylated protein A (100 μL; 100 μg mL–1 in PBS) for 1 h, rinsed with PBS, and incubated with the antibody
(50 μL; 100 μg mL–1 in PBS; in humidity
chamber) for 1 h at room temperature and then overnight at 8 °C.
On the next day, the film is rinsed with PBS buffer prior to biosensing
experiments.
Determination of Aptamer Concentration within
PSi
Quantification
of the immobilized aptamer concentration is carried out by the method
described by Hu et al.(23) for the anti-AGR2 and anti-his tag aptasensors. We used aptamers
with a thiol and FAM6 modification which are diluted in TE buffer
(10 mM Tris and 1 mM EDTA, pH 8.0), supplemented with 30 mM DTT. Prior
to use, the aptamer is cleaned in a NAP-5 column (GE healthcare),
in HEPES buffer (0.05 M HEPES, pH 7.5) to remove the DTT reducing
agent. After amino-silanization of the oxidized PSi films, the samples
are reacted with SPDP (6.5 mM in ethanol) for 30 min, followed by
washing with IPA and ddH2O three times. Anti-AGR2 (50 μM)
or 75 μM 6H7 aptamers in HEPES buffer are then introduced to
the samples and incubated for 1 h, followed by extensive washing with
HEPES, to remove physisorbed aptamer molecules. As a control, oxidized
PSi is similarly functionalized with SPDP, but without the aptamer.
The surface is washed until no fluorescence signal is detected in
the collected washing solution, compared to the control.For
the anti-AGR2 aptamer, the aptamer-functionalized PSi is incubated
with DTT solution (250 μL; 25 mM in HEPES, pH 7.5) for 30 min,
resulting in immediate aptamer cleavage from the surface by disulfide
bond reduction. The cleaved aptamer solution is collected, and the
absorbance is measured at 495 nm using a plate reader (Thermo Scientific
Varioskan), as described by Hu et al.(23) For the anti-his tag aptamer, the aptamer cleavage
from the surface is slower, attributed to the different amino silanization
procedures. Thus, the aptamer-functionalized surface is incubated
with reducing solution for 24 h, followed by solution collection and
replacement with a fresh reducing solution. This process is repeated
until no fluorescence signal is observed in the collected solution
(compared to the control). The fluorescence of the collected solutions
is analyzed using a plate reader at excitation and emission wavelength
values of 490 and 525 nm, respectively, enabling more sensitive determination
of the slower cleavage process. The measured absorbance or fluorescence
values are correlated to the respective aptamer concentrations using
a calibration curve, which is constructed using known concentrations
of the FAM6-labeled aptamer (in 25 mM DTT in HEPES buffer).
Biosensing
Experiments
Protein Targets
A 60 kDa his-tagged
protein from the
Arabinase family, named D2, and a 35 kDa his-tagged tyrosinase from B. megatherium are used as targets for the anti-his
tag 6H7 aptamer-functionalized PSi.[66] The
his-tagged tyrosinase is also detected by an anti-his tag antibody-functionalized
PSi. The 45 kDa recombinant protein A from S. aureus is used as a target for the anti-protein A aptamer,[67] and the 22 kDa AGR2 protein is detected by the anti-AGR2
aptamer-functionalized PSi.
Optical Setup
The RIFTS method is utilized for real-time
monitoring of changes occurring within the porous nanostructure by
detection of variations in the average refractive index of the porous
layer.[19,20,66] The aptamer-
or antibody-functionalized PSi sample is mounted in a custom-made
Plexiglas cell, which is fixed during the experiments to ensure that
the reflectivity is measured at the same spot throughout the experiment.
Interferometric reflectance spectra are collected with a charge-coupled
device (CCD) spectrometer (Ocean Optics, USB 4000) fitted with an
objective lens coupled to a bifurcated fiber-optic cable. A tungsten
light source is focused onto the center of the sample with a spot
size of approximately 1 mm2. Illumination and reflectivity
detection are performed perpendicular to the surface. Reflectivity
spectra are collected in real time in a wavelength range of 450–900
nm and analyzed by applying fast Fourier transformation (FFT), as
previously described by Massad-Ivanir et al.(69) The latter results in a single peak, which positions
along the x-axis, equals the effective optical thickness
(EOT) of the porous layer and is the product of the average refractive
index and the thickness of the porous layer.
Experimental Procedure
For the anti-his tag biosensor,
the surface is first washed with elution buffer for 30 min to unfold
the aptamer. Then and for all biosensing systems, the PSi biosensor
is incubated with the baseline buffer, the corresponding selection
buffer for the aptasensors or PBS for the immunosensor, for at least
30 min until a stable baseline is acquired. Next, the target protein,
diluted in the baseline buffer, is introduced and allowed to incubate
for 1 h or until a steady-state signal is obtained. Subsequently,
the biosensor is extensively washed with the baseline buffer. Throughout
the experiment, the reflectivity spectra are recorded every 15 s,
while during buffer exchange and rinsing steps, reflectivity measurements
are shortly paused.
Data Analysis
Reflectivity data
are presented as relative
ΔEOT, defined aswhere EOT0 is the averaged EOT
signal obtained during baseline establishment. For the binding curve,
the EOT used is the averaged EOT signal
at equilibration, following the wash of unbound proteins.LOD
is calculated as the protein concentration for which the optical signal
equals 3·σ, where σ is the standard deviation between
relative EOT values, measured during baseline establishment. Nonlinear
regression of obtained data was performed with GraphPad Prism software
utilizing the model for specific binding with a hill slope, according
toBmax is the interpolated
concentration at which the maximum biosensor response is reached,
and KD is the apparent dissociation constant,
which is the target concentration needed to reach the half-maximum
biosensing signal. h is the Hill coefficient, which
gives information about the stoichiometry of the binding interaction.[70,71]Table summarizes
the fitted KD values.
Numerical Simulations
We performed numerical simulations
of the governing equations using finite differences. We first discretized
the spatial derivatives using a second-order central difference approximation
with uniform grid spacing, leading to a series of coupled ordinary
differential equations. We then integrated the resulting set of ordinary
differential equations forward in time using Matlab’s routine
ode15s (Matlab R2018sb, MathWorks, Inc.). For the simulation, we used
the parameters of the aptasensors, as summarized in Table S1 (Supporting Information): a height of the solution
above the PSi of 0.001 m, a porous layer thickness of 5.5 × 10–6 m, an average pore diameter of 50 × 10–9 m, a hydrodynamic radius of the analyte of 5.3 × 10–9 m, a hydrodynamic radius of the capture probe of 3.0 × 10–9 m, a protein bulk diffusivity of 7 × 10–11 m2 s–1, a capture probe
concentration within the PSi layer of 3.6 × 10–3 M, a capture probe surface density of 1.2 × 10–8 mol m–2, a reaction association rate of 1.21 ×
103 M–1 s–1, and a
reaction dissociation rate of 6.32 × 10–4 s–1. For higher affinity interaction simulation, a reaction
association rate of 1 × 105 M–1 s–1 and a reaction dissociation rate of 1·10–4 s–1 are used.
Results and Discussion
PSi-Based
Biosensors for Protein Targets
PSi Fabry-Pérot
thin film-based biosensors are widely studied for detection of various
target molecules.[15,16] Over the past few years, we have
established several such biosensors for detection of different protein
targets[66,67] (see Table ), using both antibodies and aptamers as capture probes.
All these biosensors are based on a similar oxidized PSi nanostructure
(>70% porosity), which is ∼5 μm thick and is characterized
by interconnected cylindrical pores with an average diameter of 50
nm,[66,67] where capture probe molecules (amino-terminated
DNA aptamers or antibodies) are immobilized via different
techniques.[66,67,72,73]Biosensing experiments are performed
in a conventional cell setup, illustrated in Figure a(i), where the target protein solutions
are introduced on the top of the biosensor and incubated (without
convection). Figure b presents characteristic biosensing results for an aptasensor upon
incubation with different concentrations of the target protein, where
the EOT changes are plotted as a function of time. As the target protein
diffuses in the bulk solution toward the pore entry [Figure a(ii)], it infiltrates into
the nanostructure, diffuses, and simultaneously interacts with the
immobilized aptamer molecules [Figure a(iii,iv), respectively], resulting in an increase
in the EOT signal with time. After the EOT signal reaches equilibrium,
the biosensor is washed with buffer solution to remove nonbound target
molecules, and the attained signal is used for constructing a binding
curve. Figure c presents
characteristic binding curves for several studied capture probe–target
pairs and their corresponding curve fit, utilizing a model for specific
binding with a Hill slope.[70,71] Surprisingly, all the
investigated biosensors present a similar performance, with a dynamic
range in the lower micromolars and a measured limit of detection (LOD)
of ∼1 μM, regardless of the nature of the capture probe,
the target protein, and their binding affinity. Moreover, the apparent
dissociation constant (KD) values, as
calculated from the binding curves, are in the range of 14–31
μM, where these values are significantly higher by few orders
of magnitude from those reported in the literature, see Table . These results may suggest
that the major limiting factor of these biosensors is the porous platform
and, specifically, the involved complex mass-transfer phenomena. As
the binding behavior is similar, regardless of the theoretical affinity
between the capture probe and the target, we hypothesize that the
effect of reaction kinetics is less pronounced. However, as any measurement
is limited by the experimental setup, the signal processing method,
and, consequently, the noise of the system, these also play a role,
as has been recently suggested by Barillaro and co-workers. They applied
a different signal processing technique (named interferogram average
over wavelength, IAW) instead of the common EOT calculation, which
resulted in a significant improvement in the LOD of the PSi biosensors.[26,27] However, in the present work, we focus on the fundamental mass transfer
phenomena in PSi biosensors and study their effect on biosensing performance.
Figure 1
PSi biosensor
setup and characteristic biosensing results for different
capture probe–target pairs. (a) Schematic illustration of the
PSi biosensing system: (i) Traditional cell setup used for the RIFTS
biosensing experiments. The PSi-based biosensor is fixed in the cell
with an O-ring, confining the introduced solution to a height of H. (ii) Target solution is introduced to the cell, and target
proteins diffuse to the PSi biosensor with diffusivity Dbulk. (iii) As arriving to the pore entry, the proteins
diffuse inside the porous nanostructure with diffusivity DPSi. The PSi is functionalized with capture probe molecules
at a concentration of cB0, and the porous
layer thickness is Lp. (iv) While diffusing,
the target binds to the immobilized capture probe with kinetic parameters
of kon and koff. (b) Characteristic biosensing results presenting the relative EOT
changes with time for anti-AGR2 aptasensors upon incubation with different
concentrations of AGR2 protein solutions (n ≥
3). The relative EOT increases with the infiltration and diffusion
of the target protein into the porous layer, followed by binding to
the immobilized aptamer probes. (c) Binding curves of different protein
targets on aptamer (Ap)- or antibody (Ab)-functionalized PSi-based
biosensors, fitted with a specific binding model with a Hill slope.
The curves present a similar behavior, independent of the target protein,
capture probe, and their corresponding theoretical binding affinity.
PSi biosensor
setup and characteristic biosensing results for different
capture probe–target pairs. (a) Schematic illustration of the
PSi biosensing system: (i) Traditional cell setup used for the RIFTS
biosensing experiments. The PSi-based biosensor is fixed in the cell
with an O-ring, confining the introduced solution to a height of H. (ii) Target solution is introduced to the cell, and target
proteins diffuse to the PSi biosensor with diffusivity Dbulk. (iii) As arriving to the pore entry, the proteins
diffuse inside the porous nanostructure with diffusivity DPSi. The PSi is functionalized with capture probe molecules
at a concentration of cB0, and the porous
layer thickness is Lp. (iv) While diffusing,
the target binds to the immobilized capture probe with kinetic parameters
of kon and koff. (b) Characteristic biosensing results presenting the relative EOT
changes with time for anti-AGR2 aptasensors upon incubation with different
concentrations of AGR2 protein solutions (n ≥
3). The relative EOT increases with the infiltration and diffusion
of the target protein into the porous layer, followed by binding to
the immobilized aptamer probes. (c) Binding curves of different protein
targets on aptamer (Ap)- or antibody (Ab)-functionalized PSi-based
biosensors, fitted with a specific binding model with a Hill slope.
The curves present a similar behavior, independent of the target protein,
capture probe, and their corresponding theoretical binding affinity.
Mass Transfer and Reaction Kinetics Model
The theoretical
models, which describe the mass transfer in porous biosensors, and
specifically PSi-based biosensors, commonly apply a perfect collector
assumption to the porous layer.[28,58,59] As such, the rate-limiting step is assumed as the entry into the
pores, while the diffusion within the pores is neglected and the porous
surface is modeled as a flat capturing surface, with a capture probe
surface density of bm, as schematically
illustrated in Figure a.[28,58,74] The derivation
of such a model, named in this work as the “planar model”,
is detailed in the Supporting Information. Our aim is to investigate a complete model, which includes both
transport phenomena (to and within the pores) and reaction, as illustrated
in Figure b. To this
end, we formulate a one-dimensional model, termed in this work as
the “porous model”, describing the concentration of
the target analyte as a function of time. We refer to a conventional
cell setup with solution height H above the PSi biosensor,
a porous layer of thickness Lp, and an
average pore diameter of dp. For simplification,
we assume that the pores are stacked to each other, and we neglect
the interpore distance (consistent with the high porosity of the PSi).
The concentration of the immobilized capture probe molecules and the
introduced analyte are cB0 and cA0, respectively. We assume no convection and
one-dimensional diffusion, directed in the z axis
only.
Figure 2
Schematic illustration of the (a) planar and (b) porous models,
describing the mass transfer and reaction kinetic phenomena in the
PSi-based biosensors. The PSi has a thickness of Lp and an average pore diameter of dp. The solution height above the porous layer is H. Capture probes are immobilized at a concentration of cB0 and a density of bm. The
target analyte is introduced to the biosensor at a concentration of cA0.
Schematic illustration of the (a) planar and (b) porous models,
describing the mass transfer and reaction kinetic phenomena in the
PSi-based biosensors. The PSi has a thickness of Lp and an average pore diameter of dp. The solution height above the porous layer is H. Capture probes are immobilized at a concentration of cB0 and a density of bm. The
target analyte is introduced to the biosensor at a concentration of cA0.In the bulk solution, the time evolution of the analyte concentration, cA,bulk(z,t), is governed by Fick’s second lawSubscripts of the bulk refer to the bulk solution, where Dbulk is the analyte diffusivity coefficient
in the bulk solution.Within the porous layer, we describe the
time evolution of analyte
concentration, cA,PSi(z,t), by the diffusion-reaction equationNote that subscripts of PSi refer to the porous layer, where
the
analyte diffusivity coefficient is DPSi. This is the main difference with respect to the planar model, in
which the diffusion within the porous layer is neglected and the reaction
is only considered on the PSi surface as a boundary condition (see
the Supporting Information).We use
the standard ligand–receptor model to describe the
simultaneous reaction of the analyte with the immobilized capture
probes, and accordingly, the concentration of the bound analyte–probe
complexes, c(z,t), evolves aswhere kon and koff are the reaction
association and dissociation
rates, respectively.The governing eqs –5 are subjected
to the no-flux boundary
conditions at the ceiling of the device, on the top of the bulk solution
(z = 0), and at the bottom of the pore (z = H + Lp) (see scheme
in Figure ), as well
as the continuity of the concentration and the flux at the interface
between the bulk and the pores (z = H)andWe assume that the initial analyte concentration in the bulk
is cA0 and that the initial concentrations
of the
analyte and of the immobilized analyte–probe complexes within
the porous layer are both zerowhere
the function θ(z) is defined asThe governing eqs –5 are coupled through the boundary
conditions (6)-(9) and should be solved together to obtain the concentration
in the bulk and in the porous layer.Within the porous layer,
the constrained space of the pore leads
to hindered diffusion of the analyte molecules. Thus, the diffusivity
coefficient of the analyte within the PSi, DPSi, should be corrected according to the molecular and hindered
diffusion phenomena, accounting for steric restriction, hindered Brownian
motion, and energetic interactions of pore–solvent–analyte.[50] Empirical models for DPSi describe the hindered diffusivity as a function of the
parameter α, defined as the ratio of the hydrodynamic diameter
of the analyte dA and the diameter of
the average pore dp(z,t), that is, α(z,t) = dA/dp(z,t). The diameter of the
average pore dp(z,t) decreases upon binding of the analyte to the immobilized
probes on the pore walls and can be related to the bound analyte concentration cP throughwhere dp0 is the
initial diameter of the pore and dB is
the hydrodynamic diameter of the probe. Thus, the ratio α is
given byFor our study, we utilize the comprehensive model derived
by Dechadilok
and Deen[54] for cylindrical pores for the
estimation of DPSi
Comparison of Theoretical Models to Experimental
Results
We solve the three coupled nonlinear differential
equations numerically,
using parameters characteristic of actual PSi aptasensors, described
in Table . Specifically,
we use an average pore diameter value of 50 nm, a porous layer thickness
of 5.5 μm, and a bulk solution height of 1 mm. A representative
value of ∼7 × 10–11 m2 s–1 is applied for the protein bulk diffusivity coefficient,
based on the relative protein sizes.[75] For
the kinetic binding rate constants, we use those of the pair of anti-protein
A aptamer and protein A, which were previously determined by SPR as
1.21 × 103 and 6.23 × 10–4 s–1 for the association and dissociation rates, respectively.[62] The aptamer and target protein diameters are
3 and 5.3 nm, respectively. Please see Table S1 (Supporting Information) for a comprehensive summary of all
values used for the numerical simulations.We have experimentally
determined the concentration of the immobilized aptamers within the
porous layer, using a fluorescently labeled aptamer and its subsequent
cleavage. This method was applied for the anti-AGR2 and anti-his tag
aptasensors, and the resulting aptamer concentration ranges between
1.0 ± 0.2 and 6.28 ± 0.06 mM, respectively (see Table S2
for detailed results, Supporting Information). These values provide an order of magnitude estimation for the
probe concentration for all studied aptasensors, and thus, for the
numerical simulations, a representative value is used, that is, an
aptamer concentration of 3.6 mM.Figure a,b depicts
the real-time experimental binding curves of the investigated aptasensors
for detection of the target proteins at concentrations of 50 and 10
μM, respectively, in comparison to results obtained by numerical
simulations. We present the simulation results for the porous model
and those obtained for a planar model, where the porous layer is assumed
to be a perfect collector as is conventionally considered in the literature.[28,58,59] For the planar model (see detailed
derivation of the model in the Supporting Information), we applied the same reaction kinetic parameters and capture probe
surface density, as for the porous model. For the experimental binding
curves, the percentage of target binding was calculated by normalizing
the EOT signal to the maximal EOT signal obtained at aptasensor saturation
with the target. While our suggested porous model presents a relatively
good fit to the experimental results at both studied target concentrations,
the planar model highly overestimates the binding rate, even at a
high target concentration where mass transfer limitations should be
less pronounced (Figure a). Only at long enough times, the experimental and the model curves
converge, while at (relatively) short times, the planar model greatly
diverges. Moreover, these deviations intensify at low target concentrations,
as shown in Figure b for a target concentration of 10 μM (and in Figure S1 for
lower target concentrations of 1 and 0.5 μM, Supporting Information), mainly ascribed to the decrease in
the concentration gradient, that is, diffusion driving force, for
lower target concentrations. It should be emphasized that the porous
model fits the experimental results also when applying other reaction
rates, while the overestimation of the planar model is still apparent,
as shown in Figure S2 (Supporting Information). Our results demonstrate that hindered diffusion has a major impact
on the binding rates of PSi-based biosensors and cannot be neglected.
Thus, the porous model is essential for accurate representation of
the binding behavior, especially when studying relevant target concentrations,[76] which are orders of magnitude lower than those
presented here.
Figure 3
Comparison of experimental binding curves of the investigated
aptasensors
to numerical simulation results obtained for the porous and planar
models, at target concentrations of (a) 50 and (b) 10 μM. For
the experimental data, the EOT signals for each aptasensor were normalized
to the maximal EOT signal obtained upon aptasensor saturation with
the target. For simulated binding, the curves present the bound analyte,
normalized to the probe concentration or density, at the bottom of
the pore as a function of time.
Comparison of experimental binding curves of the investigated
aptasensors
to numerical simulation results obtained for the porous and planar
models, at target concentrations of (a) 50 and (b) 10 μM. For
the experimental data, the EOT signals for each aptasensor were normalized
to the maximal EOT signal obtained upon aptasensor saturation with
the target. For simulated binding, the curves present the bound analyte,
normalized to the probe concentration or density, at the bottom of
the pore as a function of time.To illustrate the significance of each of the diffusion phenomena,
we present, in Figure , the simulated distribution of the target concentration (in the z axis) in the bulk solution and in the porous layer, at
different time points. At the initial stage of binding, the target
is rapidly depleted near the pore entry (to a value below 5% of the
initial target concentration), and a diffusion boundary layer is formed,
spanning deep into the bulk solution. With the progress of the diffusion
of the target into the porous layer, the concentration gradient slowly
diminishes, until equilibration is reached. In contrast, for a planar
model, the depletion of the target on the biosensor surface is significantly
lower, as shown in Figure S3 (Supporting Information). These results indicate that both diffusion processes, in the bulk
and in the porous layer, are interrelated: the diffusion within the
porous layer leads to a rapid and substantial formation of a diffusion
boundary layer within the bulk solution. Thus, a similar binding behavior
observed for the different studied biosensors (see Figure c) is ascribed to the mass
transfer limitations and to the interconnected effect of both diffusion
processes. These conceal the capture probe–target protein reaction,
and our main conclusion from this study is that without significantly
accelerating the mass transfer rate, the contribution of higher affinity
capture probes for improving the biosensing performance (i.e., sensitivity and detection time) will be imperceptible. It should
be kept in mind that the system noise also plays a critical role in
determining the biosensor performance, and it should be minimized.
Thus, when applying methods for mass transfer acceleration, the resulting
LOD will also depend on their effect on the noise.
Figure 4
Simulation of the distribution
of the target concentration in the z axis at different
time points in (a) the bulk solution
and (b) the porous layer, obtained by the porous model. The target
concentration is normalized to an initial target solution concentration
of 50 μM.
Simulation of the distribution
of the target concentration in the z axis at different
time points in (a) the bulk solution
and (b) the porous layer, obtained by the porous model. The target
concentration is normalized to an initial target solution concentration
of 50 μM.We further demonstrate the contribution
of mass transfer acceleration
to the enhancement of the apparent binding rate by application of
mixing of the target solution on top of the biosensor. This results
in a constant analyte concentration within the solution above the
porous nanostructure, eliminating the diffusion gradient in the bulk
solution and decreasing the diffusion path length to the porous layer.[14] Figure S4 (Supporting Information) compares biosensing results with and without target mixing (10
min mixing followed by incubation vs incubation only).
During mixing, the EOT signal is observed to rapidly increase, and
a significantly higher apparent binding rate (by >5 fold) is obtained
in comparison to the nonmixed system, thus demonstrating the profound
effect of mass transfer acceleration on enhancing the target flux
into the porous layer. It should be noted that we use manual mixing
in this work, while a better performance in terms of sample-to-sample
reproducibility will be obtained upon mixing automation.
Effect of Biosensor
Characteristics
We use the derived
porous model to study the effect of important biosensor characteristics,
which can be tailored during the biosensor construction, on the binding
rate. The first parameter we examine is the capture probe surface
density, which is considered of high importance for surface-based
biosensors, in general,[77−80] and PSi-based biosensors, in particular.[22,23,81,82] Although for both planar and porous surfaces, an overall similar
capture probe density may be attained, the large surface area of PSi
allows immobilizing larger amounts of capture probes and their concentration
within the nanoscale pores. This in turn reduces the binding time,
affects the apparent off rate of the probe–analyte complexes,
and enhances the biosensor sensitivity, as has been previously suggested.[14,22,23] In the present work, we would
like to investigate whether an excess of capture probes within the
pores may lead to a counter effect on the mass transport rate. Figure a presents a simulation
of the effect of capture probe surface density within the porous layer
on the target binding rate for different analyte concentrations. We
apply, in the simulations, a capture probe density range of ∼10–11 to ∼10–8 mol m–2, which has been utilized in PSi-based biosensors.[23,28,81] Increasing the capture probe surface density
results in higher binding rates until an optimal surface density value;
above this value, the binding rate slightly decreases. For a higher
affinity interaction (Figure b), with an association rate of 105 M–1 s–1 and a dissociation rate of 10–4 s–1, which is characteristic for antibody–ligand
interactions,[43,83] increase in surface density results
in a drastic decrease in the binding rate. We attribute this behavior
to the decrease in the free porous volume available for the transport
of the target. In addition, at a high probe density, a depletion region
can rapidly build, which in turn will increase the thickness of the
diffusion boundary layer in the bulk (adjacent to the pore entry),[77] and as a result, both bulk and hindered diffusion
rates will decrease. Our results suggest that mass transfer limitations
require maintaining an optimum capture probe surface density, below
a certain threshold, while considering immobilization levels that
would produce a biosensor response with an acceptable signal-to-noise
ratio. This has also high significance for maintaining active probes
while immobilized, avoiding steric crowding effects.[82,84]
Figure 5
Effect
of biosensor characteristics on the simulated target binding
rate. (a,b) Effect of capture probe surface density for different
target concentrations, for low (kon =
1.21 × 103 M–1 s–1 and koff = 6.32 × 10–4 s–1) and high (kon = 105 M–1 s–1 and koff = 10–4 s–1) affinity interactions, respectively. (c,d) Effect of porous silicon
layer thickness for different pore diameters for a target concentration
of 1 μM, for low (kon = 1.21 ×
103 M–1 s–1 and koff = 6.32 × 10–4 s–1) and high (kon = 105 M–1 s–1 and koff = 10–4 s–1) affinity
interactions, respectively. The binding rate was calculated as the
slope of bound target concentration vs time curve,
in a time frame of 60 min, at the bottom of the pore.
Effect
of biosensor characteristics on the simulated target binding
rate. (a,b) Effect of capture probe surface density for different
target concentrations, for low (kon =
1.21 × 103 M–1 s–1 and koff = 6.32 × 10–4 s–1) and high (kon = 105 M–1 s–1 and koff = 10–4 s–1) affinity interactions, respectively. (c,d) Effect of porous silicon
layer thickness for different pore diameters for a target concentration
of 1 μM, for low (kon = 1.21 ×
103 M–1 s–1 and koff = 6.32 × 10–4 s–1) and high (kon = 105 M–1 s–1 and koff = 10–4 s–1) affinity
interactions, respectively. The binding rate was calculated as the
slope of bound target concentration vs time curve,
in a time frame of 60 min, at the bottom of the pore.Two additional key parameters which can be easily tailored
for
PSi biosensors are the porous layer thickness and pore diameter. These
affect both the optical properties of the nanostructure and the hindered
diffusion within the pores, as they dictate the available free porous
volume for molecular transport.[20,40,41,51]Figure c presents the effect of porous layer thickness
and pore diameter on the binding rate (as simulated at the bottom
of the porous layer), while the capture probe and the analyte concentrations
are kept constant. The results show a significant effect of the porous
layer thickness on the binding rate, with the latter decreasing for
increasing thickness. This agrees with other studies and is related
to the increase in diffusion time inside the porous layer with increasing
pore length, which scales as td ∝ Lp2/DPSi.[35,36] Thus, decreasing
the PSi layer thickness will result in an improved biosensor sensitivity.[35] The impact of the pore diameter (in the range
of 30–100 nm) on the binding rates is less pronounced. However,
this result is valid for aptasensors, where the size of the capture
probe is significantly lower than the diameter of the pores (see Table S2), whereas for larger probes (e.g., antibodies), this pore diameter range will be narrow.[33,82]When higher affinity interaction parameters are used for the
simulation
(an association rate of 105 M–1 s–1 and a dissociation rate of 10–4 s–1, typical for antibody–ligand interactions),
the effect of the layer thickness and pore diameter is intensified,
see Figure d. The
simulated binding rate decreases by orders of magnitude for the thicker
porous layer or smaller pore diameter. This is related to the impact
of the mass transfer limitation in the bulk solution and the rapid
formation of a depletion region at the pore entrance, owing to the
fast uptake of the target. Thus, for biosensing interactions with
higher affinity, the porous layer should be designed with smaller
thickness and larger pore diameter, compared to lower affinity interactions.
The number of pores in the PSi nanostructure, which can be correlated
to the PSi porosity (see derivation in the Supporting Information), also characterizes the porous layer and influences
the target capture rate. As the number of pores, and accordingly the
porosity, decreases, a higher binding rate is observed, as presented
in Figure S5 (Supporting Information).
This is related to the higher diffusion flux into each pore. Nevertheless,
the effect is less pronounced compared to the porous layer thickness
and the pore diameter, even for a high affinity interaction (see Figure
S5b, Supporting Information).It
should be kept in mind that the reflectivity of the PSi transducer,
in terms of the intensity and number of fringes (for RIFTS), highly
depends on the pore diameter and the thickness of the porous layer.[20,40,41] Figure S6 (Supporting Information) shows the experimental reflectivity
spectra for PSi films of different thicknesses, showing the decrease
in the number of fringes for thinner porous films. This in turn affects
RIFTS signal processing, whereas the reflectivity of a layer with
a thickness below 1 μm cannot be reliably analyzed. Thus, the
porous layer thickness should be as low as possible to allow high
binding rates and reflectance intensity, but this value should be
optimized to yield a sufficient number of fringes. The latter is also
dependent on the pore diameter.[39−41] The effect of the PSi structural
characteristics on the optical properties is interrelated; thus, their
collective contribution should be considered upon nanostructure optimization.[18,40] To highlight the importance of a rational biosensor design, Figure S7 presents the simulated binding rate
for various target concentrations, upon decreasing the porous layer
thickness to 2 μm and the capture probe density to 2.3 ×
10–9 mol m–2, compared to the
original PSi aptasensor. These values have been chosen according to
the simulation results of the effect of the PSi thickness and capture
probe density on the target binding rate, as presented in Figure . A significantly
enhanced binding rate is observed, suggesting that the LOD can be
improved by at least 10-fold by simply adjusting the biosensor characteristics.
Conclusions
A theoretical model, in which the complex mass
transfer processes
involved in target capture within PSi-based transducers, is derived.
The model considers the bulk diffusion of the target in the solution
toward the biosensor surface, the hindered diffusion within the porous
layer, and simultaneous reaction with the immobilized capture probe
molecules. We solve the model numerically using parameters which were
derived experimentally and are characteristic of PSi-based biosensors.
The model successfully captures the target binding rates of several
PSi aptasensors designed for protein detection, while the common-practiced
model, in which the PSi is assumed as a planar surface and thus neglects
the hindered diffusion phenomenon, drastically overestimates the target
binding rate. Numerical simulation results indicate an interrelated
effect of both diffusion processes, in the bulk solution and in the
porous layer, which cannot be separated. Thus, diffusion within the
porous layer should not be neglected, and both diffusion phenomena
are important to accurately represent the transport within PSi-based
biosensors, especially at low target concentrations. The model results
can explain ours and others encountered low sensitivity of PSi biosensors
(in the micromolar range), and similar target capture regardless of
the nature of the capture probe–target pair and their theoretical
binding affinity. Thus, accelerating mass transport, while maintaining
similar (or lower) noise levels, is essential in order to exploit
the advantages of high affinity capture probes. It should be emphasized
that although we focus, in our work, on mass transfer limitations,
system noise and signal processing methods also affect the performance
of the biosensor and should be considered for obtaining maximal enhancement
of the biosensor.The proposed theoretical model is used to
investigate the effect
of PSi biosensor characteristics, that is, capture probe surface density,
porous layer thickness, and pore diameter, which can be tailored during
biosensor construction, on the target capture rate. Importantly, we
show that the increased surface area of the PSi, which is one of the
main advantages of these nanostructured transducers, can in turn lead
to an excess of target binding sites. This results in further diffusion
impedance in the bulk solution and the porous layer. Thus, the amount
of immobilized capture probes and the corresponding surface density
should be optimized to allow an efficient mass transfer rate, while
still producing a biosensor response with a reliable signal-to-noise
ratio. Porous layer thickness and pore diameter have also high impact
on the binding rate, the latter decreasing for thicker PSi layers
and smaller pore diameters. However, the pore diameter should be large
enough to accommodate the bioreceptor and the target molecules, while
the porous layer thickness should be thinned, while allowing a reliable
optical signal processing.