Open Access Article
Swapnil Daxinia,
Chris Prüfert
b,
Paul Reida,
Pedro Barrosc,
Juan Gomez-Cruzd,
Carlos Escobedo
e,
Jack A. Barnesf and
Hans-Peter Loock
*g
aDept. of Physics, University of Victoria, Victoria, B.C., Canada V8N 5C2
bInst. of Chemistry, Physical Chemistry, University of Potsdam, 14469 Potsdam, Germany
cDept. of Biochemistry, University of Victoria, Victoria, B.C., Canada V8N 5C2
dSpectra Plasmonics, Kingston, ON, Canada K7L 0E9
eDept. of Chemical Engineering, Queen's University, Kingston, ON, Canada K7L 3N6
fDept. of Chemistry, Queen's University, Kingston, ON, Canada K7L 3N6
gDept. of Chemistry, University of Victoria, Victoria, B.C., Canada V8N 5C2. E-mail: hploock@uvic.ca
First published on 29th December 2025
The extraordinary optical transmission, EOT, through a gold-film nanohole array was used to measure refractive index changes of a thin film of polydimethylsiloxane, PDMS, upon absorption of o-xylene gas. As o-xylene diffuses into the 10 μm thick PDMS film, the film swells slightly and its refractive index increases. The PDMS index change produces a red-shift of the EOT maximum which is observable in a simple optical transmission spectrum. Since the experiments are fast (<200 ms) and precise (<2 × 10–4 RIU) we can follow the kinetics of the diffusion process with enough accuracy to distinguish two distinct diffusion mechanisms that occur at different time scales.
BTEX compounds are typically analysed using separation techniques such as gas chromatography-mass spectrometry (GC-MS), high-performance liquid chromatography (HPLC), and capillary electrophoresis (CE). Samples can be controllably enriched in BTEX concentrations using Solid-Phase Micro-Extraction (SPME), a rapid, solvent-free sample preparation method pioneered by the Pawliszyn group and others.10,11 Polydimethylsiloxane (PDMS) is a commonly used extraction matrix for SPME, as it is an elastic, chemically inert hydrophobic polymer that strongly interacts with non-polar molecules and readily absorbs BTEX from both liquids and gas samples.12 To optimize PDMS-SPME probes for optimum extraction time and film thickness, it is important to understand the diffusion kinetics of these compounds through PDMS.
The diffusion kinetics through polymers have previously been investigated through gravimetric sensors,13,14 time-lag permeation,15 and through the measurement of refractive index and swelling using a interferometric refractometer.16,17 In this paper, we present a real-time, on-line, continuous, cost-effective VOC sensing method that is based on the phenomenon of extraordinary optical transmission (EOT) to investigate the diffusion kinetics of o-xylene into PDMS.
When light is incident on an array of sub-wavelength holes in a gold or silver film, one observes higher than expected transmission for a range of wavelengths. White light from a broad band light source is thereby filtered such that some colours are blocked, and others are transmitted though the holes to an extent that is higher than expected from classical aperture theory alone.18
The EOT resonance occurs due to the photonic excitation of surface plasmon polaritons (SPPs) on the metallic surface of the noble metal film. Like surface plasmon resonance (SPR) sensors, EOT-based sensors are sensitive to the changes of the refractive index (RI) at the interface between the metal film and the dielectric medium surrounding it.18–21 They can be used to measure the refractive index of liquids22 and polymers covering the array.23 Contrary to other optical techniques that are used for VOC detection, nanohole array sensors can be interrogated in transmission mode, allowing for easier alignment, miniaturization and multiplexing.24,25 A conventional absorption spectrometer suffices for the measurement of the EOT signal. The fabrication of the device presented in this work is facile, rapid, and does not require a cleanroom.
Following the publication of the seminal work on EOT by Ebbesen et al. in 1998,18 there have been numerous sensing systems based on nanohole arrays for refractometry,20,22,26 biosensing,20,27,28 as well as in multiplexed systems.28,29 Recent work has demonstrated the use of nanohole arrays for gas detection,30,31 though the systems were based on monitoring intensity changes, rather than the plasmonic shift induced by refractive index changes, and may therefore be more prone to noise from the light source and detector. The design parameters guiding the optimization of EOT-based sensors were recently reviewed by Asif and Sahin.32
In the present study, we demonstrate the use of a PDMS-covered EOT system as a novel VOC sensing method. With the high time-resolution and high sensitivity that this sensor affords, we obtain insights into the diffusion kinetics of o-xylene into PDMS. The kinetics of o-xylene diffusion through a thin layer of PDMS are investigated by measuring the peak-shift of the plasmonic signal. To the best of our knowledge, this study is the first application of EOT spectroscopy to the measurement of gaseous analytes, representing, also, the first integration of solid-phase microextraction of gases with EOT-based plasmonic sensing.
In contrast to conventional plasmonic devices, and many previously reported EOT-based sensors, the present configuration eliminates the need for micro- or nanofabrication. The nanohole array is instead obtained by sputter-coating a commercial Transmission Electron Microscopy (TEM) support grid with a thin gold film, providing a facile and reproducible platform for optical measurements. The refractive index is obtained from an optical transmission spectrum that is recorded using a simple optical setup. The system also incorporates a compact and intuitively designed nebulizer that offers high accuracy and adjustability over a wide range of partial pressures. The diffusion model described in the SI is derived from a new and rigorous integration of Fick's one-dimensional diffusion law. A comprehensive discussion of this theoretical framework is forthcoming.
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| Fig. 1 Schematic overview of the setup with the NHA preparation, nebulization stage and optical setup. | ||
The 3D-printed chamber allows for the introduction of gas either above the PDMS layer or from the underside of the NHA. A nebulizer system was developed to generate different VOC loads in the carrier gas in a compact, resource-efficient way, allowing for adjustable and small loadings (<4000 ppm) of VOC in nitrogen gas. The dual gas-stream system can supply the chamber with only carrier gas (N2) or with analyte-containing gas from the output of the nebulizer system.
The nebulizer consists of two co-axially mounted capillaries, with the inner capillary supplying the liquid VOC through a syringe pump. Due to the steep pressure gradient, strong sheer forces are exerted on the liquid at the tip of capillary. This leads to the dispersion of the ejected liquid into a fine mist, i.e. the liquid is nebulized. The flow of heated nitrogen gas from the surrounding larger capillary carries the mist towards the sample chamber while ensuring complete evaporation of the VOC. Since the liquid and gas flow rates can be tightly controlled, the VOC partial pressure of the sample gas can be finely adjusted with about 10 ppm accuracy in the range of 10 ppm to 4000 ppm. A Computational Fluid Dynamics, CFD, simulation of the nebulizer is provided in the SI.
The depth range of the refractive index measurements is governed by the penetration depth of the surface plasmons; thus, it is essential to have strong adhesion between the PDMS and gold layer. As gold bonds only weakly to PDMS, we used (3-mercaptopropyl) trimethoxysilane (MPTMS) (Sigma-Aldrich, USA) as a molecular adhesive.33 The gold-coated NHAs were plasma-cleaned and submersed in a 10 mM ethanolic solution of MPTMS for 20 hours to produce an MPTMS monolayer. The MPTMS was then activated via plasma cleaning for 60 s before a PDMS (Dow Corning Sylgard 184, 10
:
1 mixing ratio) layer was spin-coated onto the NHA directly thereafter. The NHA was mounted onto the spin-coater, the PDMS was drop-cast onto the NHA, and spin-coated with the desired thickness – here 10 μm. The spin-coating procedure was facilitated by mounting the NHA onto a 3D-printed mount. This 3D-printed component was affixed onto the spin coater with adhesive tape. The thickness was set according to a calibration curve obtained using an optical profiler (see SI). After spin-coating, the PDMS film was cured for 10 min at 100 °C and 20 min at 70 °C on a hotplate. Since the diffusion rate of VOCs through PDMS depends strongly on the crosslinking density of the polymer film, care was taken to maintain a similar PDMS mixing ratio and preparation procedure to reproduce the crosslinking density, accurately.
The chamber holding the PDMS-coated NHA was designed in-house and resin-printed using a 3D printer. It consists of three main parts, i.e. two outer plates and one central disc with a slot that holds the NHA. The chamber was designed so that the gas exchange rate in the chamber (≈15 ms) is much smaller than the diffusion time constant (τ > 10 s), such that the PDMS diffusion governs the measurements’ response time. The plates have a 5 mm × 5 mm square open hole that is turned into an optical window using microscopy coverslip squares (Fisher Scientific, USA) that are attached and sealed using epoxy resin. On its inside face, each plate has a square center recess that forms the sample chamber. The sample chamber accepts sample gas through a bore connected with 22 needle gauge tubing to the aerosol generator, while the second bore directs the sample gas to waste after it has flown across the PDMS film which faces the white light source. The right part of the chamber (Fig. 1) has a similar design and, therefore, also permits gas flow across the silicon nitride grid that forms the support for the NHA assembly.
In the present study, all the results were obtained with the sample gas flowing through the PDMS layer towards the gold-coated NHA substrate layer as this gives better insight on the diffusion kinetics through the PDMS layer.
When reversing the gas flow from the NHA substrate towards the unsupported PDMS film surface, we observed a much faster sensor response as the analyte interacts with the plasmonic field immediately. Unfortunately, the measurements were difficult to reproduce, likely because of partial delamination of the PDMS layer due to pressure from the gas flow.
We averaged ten consecutive EOT spectra, and the average centroid wavelength is calculated with its respective standard error and with acquisition times ranging from 200 ms to 2s.
(t), of the analyte that is absorbed in the section of the film interrogated by the surface plasmon polaritons can be calculated from the film's refractive index, nmix, using (1), an equation that had been derived previously,16
![]() | (1) |
In deriving (1), it is assumed that the Lorenz–Lorentz equation holds, i.e. that molar polarizabilities, Pi, are linearly additive. Note that refractive indices, ni, are not linearly additive. In this case, we also assume that swelling of the film is negligible (Δd = 0). Although it has been observed that PDMS swells by up to 50% after 72 hours of exposure to a saturated xylene atmosphere,34 the assumption holds in our experiments, since the sorption experiments were much shorter and at a lower xylene concentration. Indeed, the maximum swelling was measured to be between 2–5% and assumed negligible for the modelling. The maximum swelling upon absorption was determined from a weak thin film interference spectrum observed in many of the EOT spectra (see SI).
![]() | (2) |
The PDMS layer on the surface is thin compared to its lateral extension, and the hole diameter is orders of magnitude smaller than the film thickness. Therefore, the problem was analysed as one-dimensional diffusion through a sheet of finite thickness having an infinite reservoir of analyte gas above the polymeric sorption film. Most of this PDMS film is supported by the gold film which is assumed to be an impenetrable substrate (described as a “supported film”), whereas a smaller fraction is suspended above the nanoholes (“free-standing film”).
We now introduce, briefly, the kinetic model of the absorption and desorption of an analyte into a thin film supported by an array of nanoholes. In our derivation we integrate Crank's solutions for a one-dimensional diffusion problem.37 When neglecting lateral diffusion, the problem can be understood as a linear combination of Crank's solution for a film mounted on an impermeable support and the solution for a free-standing film.
Eqn (4) and (6) for a supported film have been presented, previously.16 Their derivations by integration of the Crank's equations, as well as the derivation of the new eqn (3) and (5) for a free-standing film, are given in the SI. The average mole fraction of the analyte over the film sliver sampled by the evanescent wave near metal-film interface is given by
SF for a supported film (SF), and by
FSF for a free-standing film (FSF). The sliver's thickness is determined by a Finite-Difference Time-Domain, FDTD, simulation, see Fig. 2. The weighted linear combination of these contributions is determined separately for absorption processes (abs) in eqn (3) and (4) and desorption processes (des) in eqn (5) and (6). In these equations X∞ is the equilibrium mole fraction in the film, and the diffusion coefficient D is calculated from the fit to (7).
The film thickness, d = 10.2 µm was obtained using an optical profiler (see SI), and δy is the effective amplitude of the evanescent plasmonic wave into the PDMS and is obtained by modelling – see below and Fig. 2. The weighing coefficients can be estimated using the cross-sectional areas of holes (FSF) and the gold film (SF). The total sensing area is 2.0 × 105 μm2, and the nanoholes, representing the FSM, account for 4.0 × 104 μm2 or 20% of the total area. Therefore, the linear combination representing the total solvent mole fraction can be estimated as:
![]() | (3) |
A more rigorous determination of this 4
:
1 ratio, accounting for the overlap of the evanescent wave with the PDMS film, is given below and in the SI.
As will be discussed below, most processes are best analysed as concurrent sorption processes having two different diffusion rates given by D1 and D2, and (3) is therefore best written as
![]() | (4) |
![]() | (5) |
![]() | (6) |
![]() | (7) |
![]() | (8) |
The FDTD simulation was used to determine the electric field's spatial distribution across the gold surface and at various depths within the PDMS. This was used to estimate the ratio of the sensing areas between the supported film and the free-standing film in (3). Details in the SI show that the ratio is nearly identical to the 4
:
1 ratio estimated from the fractional areas in the previous section.
In addition, the integrated field intensity at the SPR resonance wavelengths was used to evaluate the decay lengths of the SPR-induced fields into the PDMS material to estimate δy = 25 nm, as the effective decay length of the evanescent plasmonic wave (Fig. 2). In this figure, the normalized average electric field intensity is calculated in 0.5 nm steps into the PDMS layer. The sinusoidal reflected field was subtracted from the average intensity to retrieve the evanescent field from the plasmonic interaction at the interface. This decay length, δy, governs the thickness of the layer in which the refractive index change can be measured, i.e. it corresponds to the bounds of the integrals that lead to eqn (3)–(6) (SI).
The wavelengths of the EOT resonances for a periodic hexagonal lattice array of nanoholes can also be approximated using momentum conservation matching conditions,42 given by
![]() | (9) |
![]() | ||
| Fig. 3 EOT resonance spectrum for solutions with different refractive indices flowing over the NHA. The arrows represent the wavelength of the resonances due to plasmonic interaction as predicted by eqn (9) for the Au–SI3N4 (gray) and dielectric–Au (gold) interfaces. As the refractive index of the solution above the Au changes, we observe a changing peak shape as the contribution of the dielectric–Au EOT resonance shifts. | ||
To perform the calibration, the NHA was placed in a PDMS mould having a 50 μm open channel to allow for the flow of calibration solutions using a peristaltic pump. Each solution was directed over the NHA for a minimum of 60 s and the average centroid wavelength for each mixture was obtained.
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| Fig. 5 Absorption and desorption curves for a nitrogen gas flow of 750 mL min−1 loaded with different concentrations of o-xylene sent through the nebulizer (with an added offset for visualization). For the first 200 s, pure N2 is flown over the chamber to establish a baseline, followed by 900 s of o-xylene/N2 flow and pure N2 flow again for absorption and desorption respectively. The data highlighted in red are also shown in Fig. 6. | ||
In order to quantify the diffusion constants of the diffusion of o-xylene into PDMS, the absorption and desorption curves were fitted separately to (3)–(6). The curves were fit (LMfit python package44) with two diffusion coefficients i.e. using a weighted sum of the respective curves (3)–(6) as expressed in (4). Fig. 6 shows an example of the least-squares fit of the absorption and desorption using 2360 ppm o-xylene (238 Pa, 8 μL min−1 flow rate) to eqn (4) having two different rates. Here, the fast and slow sorption processes were assumed to start at the same time and to occur concurrently. We note that the step in Fig. 6, and, indeed, in all sorption curves with concentrations higher than 1770 ppm indicates that concurrent absorption may not be a good model. Introducing the time delay of the slower process as an additional fitting constant gave diffusion rates that were similar but had a larger uncertainty, since the additional fitting parameter made the model less constrained. For these practical reasons we retained the assumption that the slow and fast processes start at the same time in our analysis.
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| Fig. 6 Fitting of sorption curves with diffusion eqn (8). The fit (solid red line) is a linear combination of the bi-exponential fit (dashed green and orange line) for the absorption (D1 = 3.0 × 10–8 cm2 s−1, D2 = 9.0 × 10–10 cm2 s−1) and desorption (D1 = 3.5 × 10–8 cm2 s−1, D2 = 1.9 × 10–10 cm2 s−1). The residuals are displayed below each graph. | ||
An analysis similar to that shown in Fig. 6 was conducted for all concentrations of o-xylene and the two average diffusion coefficients for each flow rate were obtained by fitting. Each datum in Fig. 7 represents the average fitted diffusion coefficients, D1, D2, of at least three runs, with the uncertainty derived from standard error. The size of the circular data markers is proportional to the asymptotic concentration, a1, a2, b1, b2, of the respective equation in (4).
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| Fig. 7 Average absorption (left) and desorption (right) diffusion coefficients (D1 and D2 given in cm2 s−1) with the dashed grey line and shaded region representing previously obtained diffusion coefficients16 for m-xylene with their uncertainties. The desorption D1 diffusion coefficient for 2062 ppm (7 μL min−1) shows a large uncertainty as not all fits were successful in capturing the second desorption process. A data table is provided in the SI. | ||
The diffusion constants for the absorption processes are averaged to D1 = (22 ± 6) × 10–9 cm2 s−1 and D2 = (0.9 ± 1.5) × 10–9 cm2 s−1, whereas averaging the diffusion constants for the desorption processes yields D1 = (29 ± 21) × 10–9 cm2 s−1 and D2 = (2.5 ± 0.7) × 10–9 cm2 s−1 (see SI for the data table Fig. 7). These values are in fair agreement with those given by Saunders et al.16 for the absorption of m-xylene into PDMS D1 = (30 ± 10) × 10–9 cm2 s−1 and D2 = (4 ± 3) × 10–9 cm2 s−1 and for the respective desorption processes D1 = (60 ± 20) × 10–9 cm2 s−1 and D2 = (5 ± 5) × 10–9 cm2 s−1.
Fig. 7 shows that even at low concentrations of o-xylene the absorption and desorption curves can be well-fit using a process having two distinct diffusion constants. A data table is given in the SI. Both diffusion constants are consistent with earlier measurements of diffusion of m-xylene (not o-xylene) into a 20 μm-thick PDMS film interrogated by glancing angle thin-film interferometry.16 The 1σ uncertainties of these previously obtained diffusion constants are given as grey bands in Fig. 7.
The more robust measurements at concentrations >1770 ppm (6 μL min−1) give diffusion constants that fall into the lower range of previously obtained values. The difference may be due to the different diffusion rates of m-xylene used previously and o-xylene used here, the slightly different composition and crosslinking densities inherent with commercial PDMS formulations, or due to different boundary layer chemistry – our PDMS film is chemically bonded to a gold film, whereas in the previous measurement PDMS was spin-cast onto glass,16 a plexiglass plate45 or a rubber membrane.46
Importantly, the observed diffusion kinetics provide further evidence for a two-stage diffusion process as first reported by Saunders et al.16 In their model, the VOC fills the pores within the PDMS resulting in a rapid change in refractive index. This process is followed by a slower absorption that changes the internal structure of the PDMS and causes it to swell. Both processes become faster with increasing VOC concentration of the surrounding gas, i.e. they are consistent with a first-order process.
The diffusion coefficients we obtained are consistent with measurements by Saunders et al. but they were 10-fold lower than those reported by other methods13,45–47 for o-xylene and its isomers. This discrepancy has been rationalized by Saunders et al. as being due to (1) the difference in PDMS manufacturers which has been shown to result in different degrees of crosslinking, thereby altering the diffusion kinetics through the polymer, and (2) the inconsistency of the mathematical modelling of the diffusion process through the PDMS, which can change the diffusion constant by a factor of 2 for different models as reported by Lue et al.13
The second point is worth emphasizing: to the best of our knowledge, eqn (4) and (6) describing the diffusion through a supported film and our new eqn (3) and (5) for a free-standing film have not been used widely before. They arise from exact integration of Crank's equations37 and are derived from the one-dimensional diffusion case described by Fick's second law (2). The more commonly used kinetic laws are usually written for the absorption process as
![]() | (10) |
![]() | (11) |
In a forthcoming publication we will discuss the diffusion models for a supported film and for a free-standing film in more detail.
These uptake and desorption measurements allowed us to determine accurate diffusion constants using equations that were obtained by an integration of Crank's equations, which in turn are exact representations of Fick's second diffusion law. The measurements are consistent with previously reported values that were obtained on a similar chemical system but with a different device. The accuracy of the diffusion constants, D, is limited by the accuracy with which we know the film thickness, d, since any fit can only obtain the rise time as a ratio of d2 and D, as apparent in the diffusion time constant
![]() | (12) |
Consider that for d = (10 ± 2) μm and an assumed D = 10 × 10–9 cm2 s−1, the uncertainty in the reported absolute diffusion constant would be 40%.
Finally, we submit that the presented device can be seen as a single receptor in an “electronic nose”, which may be combined with other receptors using different polymer extraction matrices to obtain an estimate of the chemical composition of a gas sample.
Supplementary information (SI) is available. The Supplementary Information contains details on the nebulizer design, the properties of the gold-film nanohole array (obtained by scanning electron microscopy), and the PDMS film thickness and its swelling upon o-xylene uptake. We also derive two models for the uptake and desorption of analytes into a supported film and free-standing film, respectively. Finally, we provide a FDTD calculation determining the fraction of the SPPs that interact with the PDMS near the holes and near the substrate, respectively. See DOI: https://doi.org/10.1039/d5an01181g.
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