Abstract
Proton exchange membrane fuel cells (PEMFCs), which use hydrogen as fuel, present an eco-friendly alternative to internal combustion engines (ICEs) for powering low-to-heavy-duty vehicles and various devices. Despite their promise, PEMFCs must meet strict cost, performance, and durability standards to reach their full potential. A key challenge lies in optimizing the electrode, where a thin ionomer layer is responsible for proton conduction and binding catalyst particles to the electrode. Enhancing ion transport within these sub-μm thick films is critical to improving the oxygen reduction reaction (ORR) at the cathodes of PEMFCs. For the past 15 years, our research has targeted this limitation through a comprehensive “Unravel – Engineer – Design” approach. We first unraveled the behavior of ionomers, gaining deeper insights into both the average and distributed proton conduction within sub-micron-thick films and at interfaces that mimic catalyst binder layers. Next, we engineered ionomer-substrate interfaces to gain control over interfacial makeup and boost proton conductivity, essential for PEMFC efficiency. Finally, we designed novel nature-derived or nature-inspired, fluorine-free ionomers to tackle the ion transport limitations seen in state-of-the-art ionomers under thin-film confinement. Some of these ionomers even pave the way to address cost and sustainability challenges in PEMFC materials. This feature article highlights our contributions and their importance in advancing PEMFCs and other sustainable energy conversion and storage technologies.
Graphical Abstract

Introduction.
Proton exchange membrane fuel cells (PEMFCs) offer an eco-friendly approach to power both low- and high-duty electric vehicles and a range of portable and stationary devices using H2, a fuel 3 times more energy dense than gasoline. Unlike traditional internal combustion engines, PEMFCs do not generate greenhouse gases while producing electricity. While PEMFCs have the potential to contribute to a diversified, sustainable and resilient clean energy landscape, to realize their full potential, they must hit the stringent cost-performance-durability targets set by the U.S. Department of Energy (DOE) (Table 1).1,2,3
Table 1.
Cost-performance-durability targets for PEMFCs.
| PEMFC performance criteria | LDV/HDVa | Current (2023–2024) | Target (year) |
|---|---|---|---|
| Fuel cell system cost ($/KW) | LDVb | 644 | 40 (2030); 30 (2050)2,5 |
| HDVc | 1705 | 80 (2030); 60 (2050)2,5 | |
| PGM catalyst loading (mg/cm2)d | - | > 0.4 3 | ≤ 0.3 (2030); ≤0.25 (2050)3 |
| Current density at 0.7 V (mA/cm2) | - | 0.1–1.76,7,8 | 3–4 (2030)9 |
| Power density (W/cm2) | - | 1.3910 | 1.8 (2025);10,11 >2 (2030)9,10 |
| Peak efficiency (%) | LDV | 6412 | 65 (2030); 70 (2050)2,5 |
| HDV | 645 | 68 (2030); 72 (2050)2,5 | |
| System lifetime or durability (h) | LDV | 5,000 (2030), 8,000 (2050)2,5 | |
| HDV | > 10,0005 | 25,000 (2030), 30,000 (2050)2,5 |
LDV: low-duty vehicles, HDV: heavy-duty vehicles;
numbers reported for 80-kW LDV and 275-kW HDV fuel cell systems;
PGM catalyst: Platinum-group metal catalyst.
The membrane electrode assembly (MEA) is the core of many electrochemical conversion and storage systems, including fuel cells. Fuel cells use ion-conducting polymers or ionomers in two formats. In a proton exchange membrane fuel cell (PEMFC), a proton-conducting ionomer membrane, typically several tens of microns thick, separates the anode from the cathode and enables selective proton transport from anode to cathode. The electrodes with ionomer-catalyst layers, on the other hand, serve as the sites for electrochemical reactions within PEMFCs (Figure 1a). At the PEMFC cathode, a sub-mm thick layer of ionomer glues the catalyst particles to porous carbon electrodes (Figure 1b,c).13 This ionomer layer is essential not only for binding catalyst particles to electrodes but also for conducting protons and oxygen to the catalyst interface at the cathode to facilitate the oxygen reduction reaction (ORR, O2 + 4H+ + 4e− → 2H2O). While proton transport across the bulk membrane is mostly satisfactory, proton and gas transport within the sub-μm thick ionomer layer over the catalyst particles is weak, challenges well known as “ion transport limitation” and “gas transport limitation.” As the thin ionomer binder layer conducts protons poorly to the catalyst interfaces, ORR at the cathode slows down, negatively impacting the power generation and overall PEMFC efficiency.14,15,16,17,18,19,20,21,22 Historically, research has focused on improving thick bulk ionomer membranes, but the behavior of thin ionomer films has largely been overlooked. Early stage studies suggest that proton conduction within these sub-μm thick ionomer layer at the catalyst or substrate interface differs significantly from those in bulk membrane separators.14,16,17,23,24,25 However, our understanding of the routes to the proton conduction resistance across these thin ionomer layers at interfaces is still at a rudimentary stage and needs a great deal of effort.
Figure 1.

(a) Schematic showing the basic working principle of a proton exchange membrane fuel cell (PEMFC). (b) High-resolution Transmission electron microscopy (TEM) image of the PEMFC catalyst layer13 showing ionomer-catalyst interface. Corresponding dimensions of carbon support, Pt nanoparticles and ionomer-based thin catalyst binder layer are shown below the TEM image. (c) Schematic view into the cathode catalyst layer depicting the electrochemical oxygen reduction reaction (ORR) at the cathode catalyst layer. (d) Our 3-pronged “Unravel-Engineer-Design” approach to investigate and improve ionomer thin layers on substrate mimicking catalyst binder layer of PEMFC cathode. The TEM image (b) was adapted from reference13 with permission from IOP Publishing Ltd. Copyright 2006 The Electrochemical Society.
To enhance ORR efficiency, first, an in-depth understanding of the morphological, mechanical, and ion-conduction behaviors of ionomers within sub-μm thick films and ionomer-catalyst/ionomer-substrate interfaces is critically needed. A sound, fundamental understanding of ionomer thin films and underlying interfacial phenomena can then inform and guide the engineering-based optimization of the ionomer-catalyst interfaces and new designs of ionomers aimed for catalyst layers/electrodes.
On the interfacial engineering and new ionomer design end, we need to address specific issues associated with ionomer thin films that are already identified and/or we identified through our efforts. To improve the performance at the ionomer-catalyst interfaces, by far much attention has been given to the synthesis of new catalysts,10,26,27,28 whereas a feasible and effective route to improve the thin-film proton conductivity could be engineering of the ionomer/catalyst interfaces,29,30,31,32 the exploration of which is still at its infancy and demands more focus. By alleviating the interfacial ionomer confinement through engineering ionomer-catalyst/substrate interfaces, we can create more favorable ion transport pathways through thin ionomer layer to ionomer-catalyst interfaces, improve the utilization of expensive catalysts (used Pt majorly), reduce the need for high loading of expensive catalysts, and reduce PEMFC costs, thereby.
In PEMFCs, not only the catalysts are expensive, but also the ionomers used are expensive. Currently, fluorocarbon-based and expensive ionomer Nafion is used in the membrane and catalyst binder layer. While Nafion conducts protons efficiently in bulk membranes, it offers low thin-film proton conductivity.23,29,33,34 This demands new design of ionomers which can conduct protons efficiently within thin layers at catalyst/substrate interfaces. The current reality is: ionomer design has received a great deal attention to improve membranes further. However, ionomers are rarely designed to address the challenges of catalyst-binding thin ionomer layers. Instead, ionomers are primarily designed with membrane separator issues in mind,35,36,37,38,39,40,41 and then used for binder applications as well. By designing new ionomers, if the proton conductivity within thin layers can be improved, we can achieve higher ORR efficiency with thinner ionomer layers and low catalyst loading which can cut down the costs of PEMFCs. Moreover, the environmental and health concerns of perfluorinated substance (PFAS) jeopardize the use of perfluorinated ionomers, like Nafion, in the long run. If some of the new ionomer designs can tackle cost and environmental issues, we could simultaneously address performance, cost, and sustainability challenges.
We have dedicated our efforts to these endeavors over the past 15 years realizing the gaps between current states and ultimate technical needs of PEMFCs, Over the time, we adopted a three-pronged approach with a theme “Unravel-Engineer-Design” (Figure 1d). In this feature article, we summarized our significant contributions in these three key areas: (i) Unravel the proton-conduction and other relevant properties of ionomers within sub-μm thick films as well as at ionomer-substrate or ionomer-catalyst interface; (ii) Engineer the ionomer-catalyst interface to boost ionic conductivity of thin films; and (iii) Design novel ranges of ionomers to address specific interface-related challenges. While highlighting our efforts, we have also integrated relevant work by others to explain and support our observations, providing adequate context.
UNRAVEL ionomer behavior in sub-μm thick films and at ionomer-substrate/catalyst interfaces.
Ionomers exhibit weaker ion conductivity in thin films as compared to bulk membranes.
Ionomers, in general, behave very differently in sub-micron thick films as compared to several tens of micron thick bulk membranes. Especially in PEMFCs, the ion transport limitation in thin catalyst binder layers, made of traditional ionomers, has been a common scenario.14,19 Most of the studies to unravel the ion transport limitation have been done with Nafion (Figure 2a), a fluorocarbon-based ionomer that is the current state-of-the-art proton conducting ionomer. A consistent finding by several groups is that proton conductivity is much weaker in sub-μm thick Nafion films as compared to several tens of μm-thick bulk Nafion membranes. As the thickness of ionomer films decreased, proton conductivity decreased. Yasuda45 and Karan46 both developed Arrhenius plots showing higher activation energy or barrier for proton conduction for thin Nafion films than bulk materials. For instance, the activation energy of proton conduction for ~50 μm-thick bulk Nafion membrane was 15 kJ/mol, while it was 32 kJ/mol for ~50 nm thick Nafion films at 85% RH.45,46 As the relative humidity decreased, this activation energy elevated further: 32 kJ/mol (85% RH); 50 kJ/mol (60% RH), indicating weaker proton conductivity at low %RH.
Figure 2:

(a) Chemical structure of 3M PFIA, 3M PFSA and Nafion.70 (b) Proton conductivity (σ) of Nafion thin films29 and bulk membranes.44,49 (c) Working principle of photoacid dye, 8-hydroxypyrene-1,3,6-trisulfonic acid trisodium salt (HPTS) (inset), fluorescence response of HPTS incorporated within a ~590 nm thick Nafion films.24 Here, Id and Ip are the emission intensities of HPTS at deprotonated (λem, max~510 nm) and protonated (λem, max~430–440 nm) states, respectively. (d) Id/Ip response of HPTS in 3M PFIA, 3M PFSA and Nafion thin films.70 (e) 0D GISAXS (or RSAXS) profile of Nafion films with different thickness at ~56%RH.70 (f) 2D GISAXS patterns of Nafion films with different thickness equilibrated at 100% RH.47 Here, qp and qz refer to in-plane and out-of-plane scattering vectors, respectively. (g) Schematic representation of ionic domain characteristics of thick and thin Nafion films.70 If the ionic domains are small, scattered, and poorly connected, ionic conduction will be weak irrespective of the level of water uptake. Figures regenerated by taking data from refs. 44,47,49,24,70. Figures reproduced with permission from refs. 47,70. Copyrights 2013, 2019, American Chemical Society. Copyright 2002, 2014 The Electrochemical Society.
The difference in proton conductivity between thin Nafion film and bulk Nafion membrane may vary based on the film deposition technique, but the decrease in proton conductivity with film thickness is a commonly observed phenomenon. Weber, Karan and coworkers (including Dishari) studied the behavior of sub-μm thick, self-assembled Nafion films (4–300 nm thick).44,47 A 20 nm thick, self-assembled Nafion film offered a proton conductivity of ~20 mS/cm, while it was ~93 mS/cm for bulk Nafion membrane.47 Yasuda et al.45 showed that the proton conductivity of a 100 nm thick drop-cast Nafion film was an order of magnitude lower than a ~1000 nm (1 μm) thick Nafion film. We unraveled proton conduction and other properties relevant to its hydration environment within spin-coated Nafion films23,29,48 (Table 2, Figure 2). We chose spin-coating to deposit ionomer films as this is the fastest coating method giving uniform thin films and is widely accepted. We found that proton conductivity (σ) of a ~550 nm thick, annealed Nafion film was 8.67 mS/cm at ~85% RH.29 This σ value dropped to 5.90 mS/cm for 250 nm thick Nafion films, and 2 mS/cm for 65 nm thick Nafion films (Figure 2b).29 These thin-film proton conductivity values were 1–2 orders of magnitude lower than a 25–50 μm thick bulk, freestanding Nafion membranes (80–100 mS/cm (water vapor);42,44,49 131 mS/cm (liquid water)23) Lowering relative humidity reduced proton conductivity significantly: 5.90 mS/cm (85%RH) vs. 2.2×10−4 mS/cm (25% RH) for 250 nm thick annealed Nafion films (Figure 2b).29 Together the low film thickness and low %RH had a far more detrimental effect on thin-film proton conductivity: (σ)25% RH: 2.2×10−4 mS/cm (250 nm thick Nafion film) vs. 1.04×10−5 mS/cm (65 nm thick Nafion film) (Figure 2b).29
Table 2.
Proton conductivities of perfluorinated ionomers in thin films deposited and processed under different conditions.
| Ionomer | Substrate | Electrode | Film deposition strategy | Film annealing condition | d (nm)* | % RH | λw* | (T)σ* | σ(mS/cm)* | Ref. |
|---|---|---|---|---|---|---|---|---|---|---|
| Nafion | MgO | IDE of Au | Spin coating | Unannealed | 60 | 60 | - | 25 | 3.98 × 10−4 | 33 |
| 90 | 1.58 | |||||||||
| 400 | 60 | 10−2 | ||||||||
| 90 | 2.51 | |||||||||
| Nafion | Pt-deposited SiO2 | IDE of Au | Spin coating | Unannealed | 22 | 40 | - | 25 | 5 × 10−2 | 34 |
| 95 | 12.59 | |||||||||
| 360 | 40 | 1×10−1 | ||||||||
| 95 | 31.62 | |||||||||
| Nafion | SiO2 (with thermal oxide layer) | IDE of Au | Spin coating | Unannealed | 22 | 40 | - | 25 | 1.5 × 10−3 | |
| 95 | 6.30 | |||||||||
| 400 | 40 | 3.1 × 10−2 | ||||||||
| 95 | 20 | |||||||||
| Nafion | SiO2 (with thermal oxide layer) | IDE of Au | Spin coating | Unannealed | 30 | 20 | 0.5 | 30 | 10−3 | 42 |
| 90 | 4 | 32 | ||||||||
| 20 | 0.8 | 80 | 10−2 | |||||||
| 90 | 6.3 | 75 | ||||||||
| 3M PFSA [EW: 825] |
SiO2 (with thermal oxide layer) | IDE of Au | Spin coating | Unannealed | 20 | 0.8 | 80 | 10−2 | ||
| 90 | 5.8 | 60 | ||||||||
| 3M PFIA [EW:620] |
SiO2 (with thermal oxide layer) | IDE of Au | Spin coating | Unannealed | 20 | 1 | 80 | 0.2 | ||
| 90 | 8.3 | 100 | ||||||||
| Nafion | SiO2 (with 200 nm thermal oxide layer) | IDE of Au | Spin Coating | Unannealed | 15 | 21 | 11 | 23 | 3.9×10−4 | 23 |
| 83 | 15 | 3.19 | ||||||||
| 100 | 27 | 5 | 8.0×10−2 | |||||||
| 84 | 10 | 8.31 | ||||||||
| Nafion | SiO2 (with 200 nm thermal oxide layer) | IDE of Au | Spin coating | Annealed | 60 | 24–28 | 0.07 | 25 | 1.2×10−5 | 29 |
| 83–86 | 1.1 | 1.97 | ||||||||
| 100 | 24–28 | 2.7×10−5 | ||||||||
| 83–86 | 2.83 | |||||||||
| 400 | 24–28 | 2.60×10−4 | ||||||||
| 83–86 | 7.57 | |||||||||
| 550 | 24–28 | 2.97×10−4 | ||||||||
| 83–86 | 12.4 | |||||||||
| Nafion | SiO2 (with 300 nm thermal oxide layer) | IDE of Au | Self-assembly | Unannealed | 10 | 20 | - | 60 | 2.44 × 10−3 | 43 |
| 96 | 94.86 | |||||||||
| Annealed | 20 | 1.2 × 10−4 | ||||||||
| 96 | 1.2 | |||||||||
| Nafion | SiO2/Si wafer | IDE of Au | Self-assembly | Unannealed | 4 | 20 | - | 25 | 1.41 × 10−4 | 44 |
| 95 | 24.49 | |||||||||
| 160 | 20 | 3.46 × 10−1 | ||||||||
| 95 | 44.72 |
d: film thickness, λw: hydration numbers, (T)σ: temperature at which proton conductivity was measured, σ: proton conductivity.
All proton conductivities are measured in-plane direction.
This several-orders-of-magnitude lower proton conductivity (σ) of sub-μm thick Nafion films as compared to several tens of μm thick bulk membranes is thought-provoking, and is attributed to confinement effect. When the film thickness approaches a few multiples of the radius of gyration of its polymer chains, the chains begin to experience geometric confinement.50,51,52,53 Geometric confinement is an outcome of physical entrapment of polymer chains as they are compelled to stay in low-dimension systems. The confinement effect is magnified further by interfacial interactions and interfacial processes, 14,29,24,54,55,56,57,58,59,60,291461,62,63,64,65 especially in the hydrated ionomer films. The water-ionomer-substrate interfacial interactions can pin the water and ionomers to the substrate/catalyst. Such interfacial confinement63 alongside geometric confinement53 can govern ionomer thin film behavior, making it distinctly different from bulk membranes. To be more specific, water-polymer confinement can severely affect the glass transition temperature (Tg),66,67,68 hydration behavior,24,54 water-polymer mobility,54,69 morphology,69,70 phase separation,70,71 nanoscale structural orientation,60,72 and proton conductivity47,72 thereby of hydrated ionomer films. Moreover, due to the interfacial processes, thin films end up having heterogeneous microenvironment, unlike bulk ionomer membranes.25 The heterogeneity, such as mass/density distribution of water-polymer across the thin film15,57,62,73,74,75,76,77,78 could lead to a distribution of glass transition temperature,66,67,68 water-ionomer mobility25,75 and proton conductivity23,25,29,48 across films. To gain a better understanding of thin-film proton conductivity, it is thus critical to gain a systematic understanding of the film thickness effect on the aforementioned average and distributed properties.
Fluorescence can be a powerful tool to unravel ionomer thin film properties.
We made a significant contribution to understanding the proton conduction environment within ionomer thin films by developing and extensively using a range of fluorescence-based strategies (Figure 2c,d,g, Figure 3b,d, Figure 4d-f, Figure 5, Figure 6c, Figure 9d, Figure 10d). Fluorescence-based techniques, considering qualitative, are often ignored. But they can reveal a wealth of information about polymer membranes and thin films, such as glass transition temperature,79,80,81,82,83 aging,80,82,84 ion transport dynamics,85,86,87,88 structural/orientational relaxation dynamics,89,90 and mobility.91
Figure 3:

(a) Working principle of CCVJ. The green fluorescence of CCVJ increases as it resides in a stiff environment. IRH and I0 means fluorescence intensity of CCVJ at a certain %RH and dry state, respectively. An increase in IRH/I0 thus mean a decrease in water-polymer mobility or increased stiffening/antiplasticization of ionomer films upon hydration. (b) Relative fluorescence intensities (IRH/I0) of CCVJ in a 70 nm thick Nafion film on n-SiO2 substrate and bulk Nafion (NR-212) membrane.24,54 (c) Young’s modulus of Nafion films as a function of film thickness and relative humidity.108 (d) (IRH/I0) of CCVJ in a 70 nm thick Nafion film on n-SiO2 and Au substrates.24 Figures reproduced with permission from refs. 24,54,108. Copyrights 2012, 2013, 2016, American Chemical Society.
Figure 4:

(a) Chemical structure of s-Radel, a sulfonated poly (phenyl sulfone)-based ionomer. (b, c) Neuron reflectometry is used to explore mass and density distribution across ionomer thin films. (b) NR data (symbols) and best model fits (lines in red) for 26 nm thick s-Radel films at different relative humidity conditions.75 (c) Schematic depicting water accumulation next to substrate interface of s-Radel thin films. (d-f) Time-resolved fluorescence spectroscopy of CCVJ-containing s-Radel films revealed that there is a mobility distribution across ionomer films.75 τRH and τ0 represent fluorescence lifetime of CCVJ at certain %RH and dry state, respectively. τRH /τ0 indicates the relative change of fluorescence of lifetime (or mobility) at certain %RH with respect to dry state fluorescence lifetime (or mobility). β is a stretching parameter the value of which represents mobility distribution within s-Radel thin films and increased hydration makes the microenvironment more heterogeneous in terms of mobility or stiffness. Figures reprinted with permission from ref. 75. Copyright 2018, American Chemical Society.
Figure 5:

(a) Schematic representing how incorporating HPTS helps to unravel depth-specific ion conduction in thin films and membranes using CLSM. (b) Id/Ip profiles for 68–1000 nm thick Nafion films (annealed) on glass coverslips (having SiO2 on the surface) and 35 μm thick free-standing Nafion membrane at 90% RH.25 Here, z is the distance within the film from the substrate interface, d is the film thickness. The term z/d indicates thickness (d)-normalized distance (z) from the substrate interface. Therefore, z/d values of 0 and 1 signify substrate and air interfaces, respectively. (c) Schematic representing the depth-specific phenomena giving rise to the depth-specific proton conduction environment across Nafion films. Figures 5a,b were reprinted with permission from ref. 25. Copyright 2021, American Chemical Society.
Figure 6.

(a) Schematic representation of surface engineering of SiO2 surface using a silane linker (APTES) and subsequent preparation of Nafion thin films. (b) In-plane (σIP) and out-of-plane (σoP) proton conductivities of Nafion thin films on unmodified vs. silane-modified surfaces at ~83–86% RH as function of film thickness.29 (c) Id/Ip profile of ~250 nm thick Nafion films with silane (red) or no silane (black) underneath at 90% RH.29 Films were stained with HPTS. (d) 0D-GISAXS profiles of ~250 nm thick Nafion films on unmodified- and APTES-modified substrates at 90% RH.29 (e) SEM-EDX cross-sectional images of ~150 nm-thick Nafion films on SiO2 (left) and APTES-SiO2 (right) substrates showing elemental mapping at the substrate interface (boxed regions).29 The elements S, F, N, C, and O are represented by yellow, cyan, blue, red, and green, respectively. The dimension of the boxes in which we did elemental analysis is 75 nm (height) × 1350 nm (length). (f) Storage modulus at ~20–25% RH of 50–600 nm-thick Nafion films on untreated and silane-treated surfaces respectively.29 Figures reprinted with permission from ref29. Copyright 2024, American Chemical Society.
Figure 9.

(a) Chemical structure of calix-2 ionomer. (b) In-plane proton conductivity (σIP) of Nafion and calix-2 (IEC=3.9) films with different thicknesses as a function of % RH. (c) In-plane proton conductivity (σIP) of ~15 nm thick Nafion and calix-2 films at 20–25% RH. (d, e) AFM amplitude images of ~35 nm thick films of Nafion (d) and calix-2 with IEC 3.9 (e). The scale bars shown within the images were 2 μm. (f) Proposed self-assembly modes and ionic conduction pathways within calix-2 ionomer films based on AFM and GISAXS data. (f, inset, right) GISAXS pattern of calix-2 (IEC 3.9) film at 92% RH. The solid blue arrows represent surface proton hopping, while the dotted blue arrows represent the proton conduction across individual macrocyclic cavities as well as self-assembled ion channels through multiple cavities. The green balls attached to calix[4]arene (blue) and biphenyl (red) units represent sulfonic acid (-SO3H) groups. (g) Through-plane proton conduction (Id/Ip) profile of a Nafion-calix-2 composite film (~140 nm thick) at 80% RH. The inset shows the CLSM image of the film at the film-air interface (scale bar 1 μm). The Id/Ip values at this film-air interface are shown within the dotted black box. Here the IEC of the calix-2 used to make the film was 3.9. (h) I-V curves of Nafion and Nafion-calix-2 (IEC 3.9, IEC 5.8) composite membranes were recorded in 0.1 M KCl in DI water. Figures reproduced with permission from ref. 23. Copyright 2022, American Chemical Society.
Figure 10.

(a) Chemical structure of PS-calix. (b) In-plane proton conductivity (σIP) of 150–170 nm thick Nafion, sPSf and PS-calix films at 85% RH. (c) Water self-diffusion coefficients (Dself, H2O) of Nafion, PS-calix (IEC 3, 3.85), CNTs with >1 nm and sub-nm diameters, and bulk water. Nafion and PS-calix data were obtained by us for ~300 nm-thick films at 100% RH using DOSY-NMR, while bulk water and CNT data were taken from literature for comparison.221,238,239,240,241 (d) Proton conduction profile (Id/Ip) across (a) ~140–150 nm thick PS-calix (IEC 3.85) and Nafion films measured using CLSM. The term z/d represents thickness-normalized distance within a film starting from the substrate interface. z/d of 0 and 1 signifies substrate and air interfaces, respectively. (e) %S at substrate and air interfaces of ~150 nm thick Nafion and PS-calix films obtained via elemental mapping using SEM/EDX. (f) Impedance spectra of mixed thin films containing Nafion or PS-calix with Pt nanoparticles at 85% RH. The film thickness was ~50 nm, while the diameter of Pt nanoparticles was ~ 3 nm. The ionomer-to-Pt mass ratio in the mixed suspension used to make the films was 10: 0.013. (g) TEM/EDX elemental maps (Pt, O, S, C, and overlay) of ~50 nm thick PS-calix (IEC 3.85, top panel) and Nafion films (bottom panel) in which Pt nanoparticles were dispersed. The scale bar was 50 nm. Figures reprinted with permission from ref.48, Copyright 2023, Cell Press.
For instance, by staining ionomer films with fluorescent photoacid dyes, we were able to measure the extent of proton conduction (deprotonation ratio), local proton concentration and pH within ionomer films. We also showed that the deprotonation ratios nicely complement the quantitative values of proton conductivity (σ), measured using electrochemical impedance spectroscopy (EIS) (Figure 2d vs. 2b, discussed in detail in the next section), validating the reliability of fluorescence-based techniques. In fact, fluorescence offered insights that traditional thin-film characterization methods could not. For example, we revealed both average24,29,47,69 and location-/depth-specific23,25,29,48 proton conduction behavior across ionomer films. These are unique information for the energy research community and especially valuable for ionomer thin films whose properties can vary significantly at different interfaces, unlike free-standing bulk membranes. In our work, we particularly stained ionomer films with fluorescent dyes sensitive to local pH, proton concentration, extent of proton conduction and mobility, and leveraged steady state fluorescence spectroscopy, time-resolved fluorescence spectroscopy, and confocal laser scanning microscopy (CLSM) to investigate key properties. The goal was to understand the water-polymer mobility,24,54,69,75 ionic domain characteristics,69,70 hydration-induced plasticization,24,25,54,69,75 and average-24,29,47,69 and distributed23,25,29,48 proton conduction behavior23,24,25,29,47,48,69 across ionomer films. We also performed traditional morphological, mechanical, and electrochemical characterizations simultaneously, and combined with the observations from fluorescence-based techniques to better understand what happens under thin film confinement. We extended this combined approach to a wide range of fluorocarbon- and hydrocarbon-based ionomers. This feature article captures some of our key observations so far about ionomer thin films through these attempts.
Fluorescent photoacid dyes can reliably inform about local proton conduction environment and help understand quantitative values of proton conductivity (σ).
We stained a series of sub-μm thick ionomer films with a fluorescent photoacid dye, 8-hydroxypyrene-1,3,6-trisulfonic acid trisodium salt (HPTS) and exposed the films to different %RH23,24,48,70 to probe the change in proton conduction environment. HPTS has a phenolic -OH group that responds to local proton concentration via protonation/deprotonation (Figure 2c, inset). At dry or low humid state, the phenolic -OH does not dissociate and emits blue fluorescence (Ip) from its protonated state. But when the film is hydrated and the surrounding hydration environment of HPTS becomes favorable for proton conduction, HPTS donates its phenolic proton (-OH ↔ -O− + H+), and the proton is carried away from the proton generation site by water molecules and ionomer’s ion-conducting groups. The deprotonation of HPTS in a strongly proton-conducting environment thus emits green fluorescence (Id). The ratio of green-to-blue fluorescence (Id/Ip) from HPTS gives an indirect measure of extent of proton transport. We observed that Id/Ip increased with the increase in %RH (Figure 2c) and film thickness (Figure 2d).
σ, on the other hand, is the typical measure of quantitative value of proton conductivity, obtained using EIS. We revealed that s and Id/IP scales with each other and give complementary information. Just like we saw a decrease in proton conductivity (s, Figure 2b), we saw a decrease in Id/Ip ratio as the Nafion films became thinner (Figure 2d). For instance, Id/Ip of Nafion film decreased from 0.70 to 0.29 as the film thickness decreased from 470 nm to 150 nm (Figure 2d),70 while s decreased from 8.18 mS/cm to 3.89 mS/cm for Nafion films with similar thickness (Figure 2b).
Proton conduction environment in fluorocarbon and traditional hydrocarbon-based ionomers can be different:
We extended the developed HPTS-based technique to study thin film behavior of a series of perfluorinated ionomers: 3M PFIA, 3M PFSA and Nafion (Figure 2a).70 We observed that Id/Ip decreased as the ionomer film thickness decreased irrespective of the type of ionomer studied. Also, the Id/Ip of HPTS embedded within ionomer films followed the trend: 3M PFIA > 3M PFSA > Nafion (Figure 2d), similar to what was reported for these ionomers in bulk membranes.39,92,93 While there can be various influencing factors, the proton conductivity trends of these three ionomers aligned with the expected impact of ionomer chemical structure on proton conduction. 3M PFIA, 3M PFSA and Nafion have the same fluorocarbon-based backbone, but their side chains are not the same. All of them have one perfluorosulfonic acid (-CF2SO3H)-based proton-conducting group per side chain, while 3M PFIA has an additional proton-conducting group, bis sulfonyl imide (Rf-SO2-NH-SO2-Rf). The Gibbs free energy of acid dissociation (also known as gas-phase acidity) of bis sulfonyl imide group (ΔGacid =284.1 kcal/mol)94 is lower than perfluorosulfonic acid (ΔGacid =299.5 kcal/mol).94 With two proton-conducting groups per side chain, including one highly acidic, 3M PFIA thus emerged as the strongest proton conductor in this fluorocarbon-based ionomer series, as reflected in the Id/Ip values, even under thin-film confinement70 (Figure 2d).
To avoid toxic perfluoro substances and cut down ionomer costs, hydrocarbon-based ionomers are designed. However, sulfonated polysulfone (sPSf), a leading hydrocarbon-based ionomer, exhibited negligible green fluorescence (Id) and the lowest Id/Ip ratio,95 matching with its low thin-film proton conductivity (σ: 9 mS/cm (Nafion) vs. 0.2 mS/cm (sPSf), 150 nm thick unannealed films on Au/SiO2, 85%RH).48
Overall, these Id/Ip - σ studies revealed that commonly known ionomers (both fluoro- and hydrocarbon-based) conduct protons poorly in thin films. Additionally, some of the well-known hydrocarbon-based ionomers (e.g., sulfonated poly(ether ether ketone) (sPEEK), sulfonated poly(sulfone) (sPSf)), conducting proton efficiently in bulk membranes,96 fail badly to conduct protons in sub-μm thick films. This negatively impacts the performance (current density, power density, ORR kinetics) in membrane electrode assemblies (MEAs) (Table 3).18,19,20,21,22,97,98,99,100,101,102,103 Understanding why these occur is crucial for improving electrode design and ORR efficiency. After being barely touched for decades, understanding in this area is now gradually evolving. In this section, we briefly discussed the effect of the chemical structure of ionomers, but there are many other factors that impact the thin-film proton conductivity in a complicated manner. We thus put efforts into identifying those other factors responsible for poor proton conductivity in thin films.
Table 3.
Summary of hydrocarbon-based ionomer performances reported for cathode catalyst layers or membrane electrode assemblies (MEAs).
| Membrane ionomera | Cathode binder ionomera | Binder ionomer IEC* (meq/g)/ DS (%) | Binder ionomer content (wt% or mg/cm2) | Binder ionomer/ carbon ratio (I/C) | Cathode Catalyst loading (mg/cm2) | Cathode Catalyst/ support (wt ratio) | Operating conditions | Current density at 0.7 Vb (A/cm2) | Power density at 0.7 Vb (W/cm2) | Ref. |
|---|---|---|---|---|---|---|---|---|---|---|
| Nafion | Nafion | n.a.* | n.a. | - | 0.05 | PtCo/C | 94 °C, H2/air 65% RH, 2.47 atm | 1.125 | 0.78 | 8,151 |
| 0.1 | 1.25 | 0.875 | ||||||||
| 0.2 | 1.65 | 1.16 | ||||||||
| Nafion | Nafion | n.a. | n.a. | - | 0.05 | PtCo/C | 80 °C, H2/air 100% RH, 1.48 atm | 0.7 | 0.49 | 8 |
| 0.1 | 1 | 0.7 | ||||||||
| 0.2 | 1.2 | 0.84 | ||||||||
| Nafion 211 | Nafion D520 | 1/- | 30 wt% | - | 0.4 | Pt/C | 80 °C, H2/O2 100% RH, 1 atm | 0.85 | 0.595 | 36 |
| Nafion 211 | sPEEK | 1.4/- | 30 wt% | - | 0.4 | Pt/C (46/54) | 80 °C, H2/ O2 100% RH, 1 atm | 0.115 | 0.081 | 101 |
| Gore M735.8 | Nafion D2021 | 0.92/- | 28 wt% | 0.4 | Pt/C (40/60) | 80 °C, H2/air 100% RH, 1 atm | 0.47 | 0.33 | 162 | |
| PFSA 1050 EW* | PFSA 1050 EW | 0.95/- | 31 w% | - | 0.4 | Pt/C (40/60) | 80 °C, H2/air 75% RH, 1 atm | 0.18 | 0.126 | 19 |
| PFSA 750 EW | PFSA 750 EW | 1.33/- | 31 wt% | - | 0.2 | 0.14 | ||||
| Nafion 112 | sPEEK 550 W | 1.8/- | 31 wt% | - | 0.02 | 0.014 | ||||
| PFSA 750 EW | PFSA 750 EW | 1.33/- | 24 wt% | - | 0.2 | 0.14 | ||||
| Nafion 112 | sPEEK 750 EW | 1.33/- | 15 w% | - | 0.075 | 0.053 | ||||
| Nafion 112 | sPSU 650 EW | 1.54/- | 15 w% | - | 0.06 | 0.042 | ||||
| sPEEK (IEC 1.75) | Nafion | 0.91/- | 30 wt% | - | 0.4 | Pt/C | 80 °C, H2/ air 75% RH, 1 atm | 0.05 | 0.035 | 21 |
| sPEEK | 1.35/- | 0.022 | 0.015 | |||||||
| 1.75/- | 0.022 | 0.015 | ||||||||
| 2.1/- | 0.04 | 0.028 | ||||||||
| Nafion 112 | Nafion 112 | 0.91/- | n.a. | - | 0.2 | Pt/C (20/80) | 60 °C, H2/ O2 75% RH, 1 atm | 0.3 | 0.21 | 163 |
| sPSU-P50 | 0.95/- | 0.2 | 0.14 | |||||||
| sPEEK | Nafion | 0.91/- | 45 wt% | - | 0.4 | Pt/C (40/60) | 75 °C, H2/air 100% RH, 1 atm | 0.25 | 0.18 | 98 |
| sPEEK | 1.74/- | 40 wt% | 0.185 | 0.13 | ||||||
| sPEEK | 1.74/- | 10 w% | 0.1 | 0.07 | ||||||
| Nafion 112 | Nafion | 0.91/- | 30 w% | - | 0.48 | Pt/C (60/40) | 65 °C, H2/air 100% RH, 1.4 atm | 0.4 | 0.28 | 97 |
| Nafion 112 | sPEEK | 1.88/65 | 0.12 | 0.084 | ||||||
| Nafion 112 | sPEEK | -/60 | 30 wt% | - | 0.3 | Pt/C (60/40) | 65 °C, H2/air 100% RH, 1 atm | 0.095 | 0.067 | 100 |
| sPEEK (IEC 1.9) | Nafion | 0.91/- | 30 wt% | - | 0.25 | Pt/C (20/80) | 50 °C, H2/O2 100% RH, 1 atm | 0.3 | 0.21 | 102 |
| sPEEK | 1.9/- | 10 wt% | - | 0.14 | 0.098 | |||||
| sPEEK | 1.9/- | 30 w% | - | 0.14 | 0.098 | |||||
| sPEEK | 1.9/- | 40 wt% | - | 0.05 | 0.035 | |||||
| sPEKK (IEC 1.4) | Nafion | 1.4/- | 25 wt% | 0.4 | 80 °C, H2/O2 75% RH, 1 atm | 0.625 | 0.44 | 164 | ||
| Nafion 112 | sPE | 1.61/- | - | 0.7 I/C | 0.5 | Pt/C (45.8/54.2) | 50 °C, H2/O2 100% RH, 1 atm | 0.5 | 0.35 | 152 |
| 2.17/- | 0.54 | 0.38 | ||||||||
| 3.73/- | 0.24 | 0.17 | ||||||||
| Nafion 117 | Nafion | 0.91/- | 30 wt% | - | 0.25 | Pt/C (20/80) | 35 °C, H2/air 100% RH, 2.04 atm | 0.058 | 0.04 | 99 |
| sPEEK | 1.88/67 | 0.013 | 9.1×10−3 | |||||||
| Nafion 112 | sPE | 1.61/- | - | 0.7 I/C | 0.5 | Pt/C (45.8/54.2) | 70 °C, H2/O2 100/25% RH, 1 atm | 0.225 | 0.16 | 152 |
| 2.17/- | 0.34 | 0.24 | ||||||||
| 3.73/- | 0.275 | 0.19 | ||||||||
| Nafion 112 | sPE | 2.17/- | - | 1 I/C | 0.5 | Pt/C (45.8/54.2) | 70 °C, H2/O2 100/25% RH, 1 atm | 0.26 | 0.18 | 152 |
| Nafion 117 | sPES-40 | 1.59/- | 0.9 mg/cm2 | - | n.a. | n.a. | 70 °C, H2/O2 100% RH, 3 atm | 0.5 | 0.35 | 103 |
| sPES-40 | sPES-40 | 0.3 | 0.21 | |||||||
| Nafion 112 | sPAE | 2.5/- | - | 0.7 I/C | 0.5 | Pt/C (48/52) | 80 °C, H2/O2 100% RH, 1 atm | 0.15 | 0.105 | 165 |
| 2.5/- | Pt/C (68/32) | 0.25 | 0.175 | |||||||
| 1.8/- | Pt/C (68/32) | 0.2 | 0.14 | |||||||
| Nafion 212 | BPS-27k | n.a. | 20 w% | - | 0.4 | Pt/C (46.2/53.8) | 80 °C, H2/O2 100% RH, 1 atm | 0.5 | 0.35 | 166,.154 |
| sPAES | BPS-27k | 0.3 | 0.21 | |||||||
| PES | PES | 1.43/- | 2 w% | - | 0.4 | Pt/C (40/60) | 70 °C, H2/O2 100% RH, 1 atm | 0.115 | 0.081 | 167 |
| 32 wt% | 0.025 | 0.018 | ||||||||
| F-PES | F-PES | 1.28/- | 2 w% | - | 0.4 | Pt/C (40/60) | 70 °C, H2/O2 100% RH, 1 atm | 0.1 | 0.07 | 167 |
| 32 wt% | 0.06 | 0.042 | ||||||||
| sPPP | sPPP | 2.17/- | 20 w% | - | 0.4 | Pt/C | 80 °C, H2/O2 95% RH, 1 atm | 0.13 | 0.091 | 155 |
| 3.70/- | 0.74 | 0.518 | ||||||||
| sPPB | sPPB | 3.23 | 7.5 wt% | 0.4 | Pt/C (46.5/54.5) | 80 °C, H2/O2 100% RH, 1 atm | 0.80 | 0.56 | 168 | |
| sPPB | sPPB | 3.19/- | 15 wt% | - | 0.4 | Pt/C | 80 °C, H2/O2 100% RH, 1 atm | 0.65 | 0.455 | 22 |
| 30 wt% | 0.25 | 0.175 | ||||||||
| Nafion 112 | sPI | n.a. | 0.5 | 0.5 | Pt/C (46.3/53.7) | 70 °C, H2/O2 100% RH, 1 atm | 0.4 | 0.28 | 169 | |
| NEXAR | NEXAR | 1 | 33 wt% | - | 0.52 | Pt/C (66.7/33.3) | 80 °C, H2/ O2 100% RH, 1 atm | 0.25 | 0.18 | 156 |
| Pemion | Pemion | 3.1 | 9 wt% | 0.2 I/C | 0.4 | PtCo/C (45.3/54.7) | 80 °C, H2/O2 95% RH, 2.47 atm | 1.25 | 0.875 | 105 |
| 80 °C, H2/air 95% RH, 2.47 atm | 0.6 | 0.42 | ||||||||
| Nafion® 212 | Spiro 30 | 29.1 | 5 wt% | 0.4 | Pt/C (46.5/53.5) | 65 °C, H2/ air 95% RH, n.a. | 0.035 | 0.02 | 170 | |
| Nafion 212 | Nafion | 1 | n.a. | 0.8 | 0.07 | Pt/C (40/60) | 80 °C, H2/O2 95% RH, 2.47 atm | 0.5 | 0.35 | 171 |
| SDT COF-Nafion | 1.70 (COF)/- | 1.5 | 1.05 | |||||||
| Nafion 212 | Nafion | 1 | n.a. | 0.8 | 0.07 | 80 °C, H2/air 95% RH, 2.47 atm | 0.25 | 0.175 | 171 | |
| SDT COF-Nafion | 1.70 (COF)/- | 0.5 | 0.35 | |||||||
| U.S. DOE Target | ≤ 0.3 (2030); ≤0.25 (2050)3 | 1.07 (2023)5 3–4 (2030)9 | 1.8 (2025)10,11 >2 (2030)9,10 | 3,5,9,10,11 | ||||||
n.a. = information not available; EW = equivalent weight = 1000/IEC, where IEC = ion exchange capacity.
PFSA= perfluorosulfonic acid, sPEEK = sulfonated poly(ether ether ketone), sPEKK = sulfonated poly (ether ketone ketone), sPE/sPSU/sPAE/ sPES/ sPAES/ BPS = derivatives of sulfonated poly (arylene ether sulfone), sPPP = sulfophenylated poly(phenylene), sPPB = sulfophenylated poly(phenylene) biphenyl, PES = sulfonated poly (ether sulfone), F-PES = fluorinated poly (ether sulfone), sPI = derivatives of sulfonated polyimide, Nexar = sulfonated styrene-based pentablock terpolymer, Pemion = derivative of sulfophenylated poly(phenylene), Spiro = derivative of poly(arylene ether sulfone) containing spirobiindane groups.
Current and Power density is reported at 0.7 V because a fuel cell typically generates a voltage from 0.6–0.7 V at a full-rated load.
Ionic domain size and connectivity matter more than water uptake.
A common school of thought is higher water uptake should lead to higher proton conductivity. The reason is water facilitates proton hopping. However, our study of hydration number (λw, moles of water/moles of proton-conducing groups) of ionomer thin films revealed something interesting. We repeatedly showed for many ionomers that there is no straightforward correlation between hydration number (λw) and proton conduction behavior (Id/Ip and σ) of ionomer thin films.23,48,24,70 For instance, a 70 nm thick Nafion film showed λw similar to a 50 μm thick bulk Nafion membrane.24 However, the Id/Ip value was an order of magnitude lower in the thin film as compared to the bulk membrane.24 These facts indicated that there may be factors other than water uptake which control the proton conduction in sub-μm thick, confined ionomer films.
We found that thinner, spin-coated films of fluorocarbon-based ionomers (3M PFIA, 3M PFSA, Nafion) had higher degree of phase mixing from TEM images.70 Also, thinner films did not show any significant scattering, suggesting a loss of correlation between ionic domains in the polymers in both 0D-GISAXS (Figure 2e)70 and 2D-GISAXS47 studies (Figure 2f). We generated a calibration curve showing Id/Ip response of HPTS in aqueous solutions with different acid (HCl) concentration and used this curve to predict the proton concentration in HPTS-stained films of 3M PFIA, 3M PFSA and Nafion by comparing the Id/Ip values.70 A similar method was adopted earlier to understand membranes by Fayer et al.104 What we found that as the film thickness and %RH decreased, proton concentration ([H+]) in the ionic domains increased suggesting protonic confinement within ionic domains and poor connectivity between ionic domains.70 Later, by comparing the Id/Ip response of HPTS in reverse micelles and ionomer films, we found that the average size of ionic domains in sub-μm thick ionomer film (~1–2 nm) is smaller than that in bulk membranes (4 nm).70 Moreover, the size of ionic domains in films of all three ionomers, independently obtained from RSAXS and steady-state fluorescence, closely matched.
Together these facts tell a story. Proton transport requires long-range, connected pathways achievable through formation of well-connected, large hydrophilic phases or ionic domains. In an ideal scenario, proton conduction happens through Grotthuss mechanism, where water molecules form H-bonded network to create a continuous pathway for proton hopping. However, if the ionic domains are small, scattered, and ill-connected (as seen in TEM, GISAXS, fluorescence studies), ion hopping, and ionic conduction weakens despite high water uptake (Figure 2g). This is likely what happens in thinner Nafion and other fluorocarbon ionomer films and explains their weak proton conductivity in thin films. The hydrophilic-hydrophobic phase mixing and disconnect between ionic channels in thin films could be far more severe in hydrocarbon-based ionomers explaining why traditional hydrocarbon-based ionomers exhibit conductivity48,95,105 much lower than fluorocarbon-based Nafion. For instance, the in-plane proton conductivity of binder-phase was reported as 10 mS/cm, 1.12 mS/cm and 0.7 mS/cm when PFSA, sPEEK and sPSf were used as binder ionomer, respectively.19 This also explains why traditional hydrocarbon-based ionomers suffer more from catalyst binder-phase diffusion limitation,18,19 sluggish ORR kinetics,102,103 and lower power density20 compared to fluorocarbon-based MEAs (Table 3, power density at 0.7 V). For example, at ~30 w% ionomer loading in Pt/C-based binder phase, the power density of MEA at 0.7 V was reported as 0.60 W/cm2 for Nafion (membrane)-Nafion (binder),36 whereas 0.08 W/cm2 for Nafion (membrane)-sPEEK (binder)101 at comparable conditions (80 °C, H2/O2, 100 %RH, 1 atm).
Kreuer106,107 and later Holdcroft105 held similar factors (less acidic side chains, poor phase segregation, narrower and less connected ionic channels with more dead ends) responsible for explaining the weaker transport behavior of hydrocarbon-based ionomers than fluorocarbon-based ionomers even in bulk membranes at low humidity conditions, where also protonic confinement is obvious. These findings suggested that controlling the size and connectivity of ionic domains is crucial for improving thin film ionic conductivity.
Polymer chains and water molecules are pinned to the substrate and lose mobility in thin films.
Another important observation we made is: ionomer chain and water mobility are sacrificed in thin films. This is a combined effect of both thin-film confinement and interfacial interactions. The thin-film confinement effect was evident when the mobility or stiffness of bulk, free-standing Nafion membrane was compared with a sub-μm thick Nafion film on the substrate. This was effectively probed by staining Nafion samples with a rotor probe (9-(2-Carboxy-2-cyanovinyl)julolidine, CCVJ) the green fluorescence of which intensifies when it resides in a stiff or less mobile environment (Figure 3a). As can be seen, a 70 nm thick Nafion film experienced hydration-induced antiplasticization or stiffening at 25–30% RH (i.e. (IRH/I0)25–30% RH > (IRH/I0)dry state), whereas a 25 mm thick Nafion membrane did not show any sign of antiplasticization, rather the film softened over the entire humidity range (Figure 3b).24,54 The stiffening of thinner films was in agreement with the modulus data obtained by Soles et al.(Figure 3c),108 Weber et al.109 and later by us29,48 where the modulus of Nafion films increased as the films became thinner. Similar hydration-induced stiffening was observed for s-Radel (Figure 4a) in thin films using CCVJ and time-resolved fluorescence (discussed later, Figure 4).75
Unlike bulk, free-standing, bulk membranes, thinner ionomer films experience a substrate interface. Therefore, the observed stiffness is not only a thickness-induced effect but also induced by ionomer-water interactions with substrate on which thin films were made. For example, a Nafion film made on a highly interactive substrate (e.g., on native oxide of silica (n-SiO2)) sorbed more water and stiffened more than a Nafion film with similar thickness but made on a less-affine substrate (e.g. Au) (Figure 3d).24 The -SiOH groups of silica-based substrates (with native/thermal oxides) can form H-bonds with -SO3H groups of ionomer side chains and water (H2O). There can also be electrostatic interaction between -SO3− groups of ionomers and hydronium ions (H3O+), seen for Nafion films on both SiO214,24,54,64,110 and Pt/PtO. 14,55,56,57,58,59,61,62,65,111,112 Such interactions can pin the ionomer chains and water molecules to substrate and limit their mobility in thin films.24,54 On the contrary, Au has lower affinity to -SO3H and water as compared to SiO273 and acts as a less restrictive surface than SiO2 (proven by Tg - studies63). The lower magnitude of interaction thus caused less chain pinning to substrate and less stiffening of Nafion films on Au (Figure 3d). Also, On a relevant note, higher water uptake by films (Nafion24 or s-Radel75) on interactive substrates may be tied to the formation of water-rich layers near the substrate, seen consistently using neutron reflectometry (NR) by Dura,73,74,75 Decaluwe74,76 Karan,15,78 Dishari,75 Inukai,57,77 Yager,113 and others62 (discussed in next section).
Distribution of ionomer chains and water across the film is heterogenous across thin films.
In sub-mm thick films, the mass distribution of ionomer and water is not the same across ionomer films. Neutron reflectometry (NR)57,73,74,75,76,113 revealed that in hydrated films, ionomer chains form several nm-thick lamellar layers next to substrates (SiO2, Au, Pt, C) which are often water-rich, and the rest of the film is more bulk-like with random ionomer-water distribution. The number, thickness, and composition of lamellar layers in ionomer thin films were found to be dependent on the nature of ionomer,15,73,74,75 film thickness,74,75 interactive nature15 and roughness76 of substrate57,76,114 on which the films were made, and hydration level. For example, Nafion films are reported to have multiple water- and polymer-rich lamella layer next to thermal SiO2 substrate,73,74 whereas s-Radel (Figure 4a) films only had one thin water-rich layer next to substrate (Figure 4b,c).75 Karan et al.15 suggested a correlation between ionomer side chain length and thickness of interfacial water layer, whereas DeCaluwe et al.76 showed that hydrophilic and smooth substrate interfaces favored lamellar phase segregation more. Dura, DeCaluwe and co-workers (2018)74 also showed that the water volume fraction in the interfacial lamellar layer is higher than that in the bulk layer in ≥60 nm thick Nafion films on SiO2. The plausibility of such a scenario was suggested by Dishari and Hickner (2012)54 from hydration number (λw) and rotor probe-based studies (IRH/I0), i.e., a high volume fraction of water accumulating in lamellar zones next to substrate is likely leading to higher water uptake by thin films and its antiplasticization. Additionally, Hickner (IR, ellipsometry),60,110 Kusoglu (3D GSAXS),14,64,65 Notsu (sum frequency generation (SFG) spectroscopy),77 Lee (simulation)111 and many others (2014-) showed that in the next-to-substrate (SiO2, Pt) region, ionomer (Nafion) chains preferentially orient their backbones parallel to the substrate, while their side chains (-SO3H-terminated) face the substrate. These individual studies supported each other and together suggested that such chain orientation favors interfacial interactions among silanol (-SiOH) groups of substrate, water, and -SO3H groups of Nafion chains lying flat on the surface. As a result, ionomer chains and water get pinned to the substrate,24,29,54,115,116,117 lose mobility,24,54,69,75 and stiffen the films.24,29,48,54,109, 115 Nafion films on Au and Pt also showed heterogeneous water distribution62 and interfacial water accumulation.73,111 However, the compositions of interfacial layers in Nafion films on different substrates were different.73 For example, Au accumulated less water next to it than SiO2. Since water plays a big role in inducing interfacial interaction, Nafion films on Au stiffened less than Nafion films on SiO2 (Figure 3d).24
Average ionomer properties do not tell the full story - Thin-film properties can be distinctly different at different depths and interfaces.
Understanding of ionomer thin films evolved over time, but took a turning point, when new tools were explored to study distributed properties, alongside average properties for the entire film. The understanding of depth-specific properties is critical for thin films as unlike bulk systems, thin film behavior can be locally influenced by different interfaces. Especially, many unique processes occur at the ionomer-substrate interface the effect of which can propagate across the film and modulate ionic conductivity and many other properties across the film. For a long time, this aspect of ionomer films remained largely unexplored as traditional ionomer characterization strategies, except a few, give average properties only. Of these few strategies, are neutron reflectometry (NR),57,73,74,75,77 X-ray computed tomography (X-ray CT),118,119 cryo-TEM tomography,120 and resonant soft X-ray scattering (RSOXS)121,122,123 have elucidated the mass/density distribution,57,73,74,75,77,118,119 3-dimensional chemical121 and nanostructure119,120,121 within heterogeneous materials. However, many of these strategies require intense modeling efforts which also require extensive expertise to interpret ionomer properties reliably and meaningfully. On top of that, these instruments are not often accessible for routine, everyday use which is critical for material exploration at nanoscale to expedite energy materials discovery. Fluorescence79,124,125 and ellipsometric68 techniques are often employed to unravel the Tg- distribution across polymer thin films. However, ion conduction44 and mechanical properties,108 the two key performance parameters of ionomers, are still reported as an average value for entire samples. Therefore, effective strategies are critically needed to reveal the distribution of these properties across ionomer samples.
Dishari put significant efforts into addressing these needs. In one effort, Dishari et al.75 revealed time-resolved fluorescence properties of CCVJ incorporated in s-Radel thin films (Figure 4d-f). A remarkable decay in the lifetime of CCVJ was found for the thicker films at high hydration condition, while it was not the case for thinner s-Radel films (Figure 4e). This confirmed hydration-induced antiplasticization and higher confinement in thinner s-Radel films. The fluorescence decay of CCVJ in s-Radel film was fitted to a stretched exponential function, where β is a stretching parameter (0 ≤ β ≤1). β tells about the distribution of fluorescence lifetime (τ). The value of β approaches 1 as the mobility within the hydration environment becomes more homogeneous. Interestingly, as we gradually hydrated s-Radel films, β values moved away from 1 (Figure 4f) suggesting mobility distribution becoming more and more heterogeneous. This made us realize that there is a distribution of hydration environments across ionomer films and thus proton conduction and other relevant properties can also be heterogeneously distributed across ionomer films. In our work, we thus routinely looked beyond the average properties by developing a robust, everyday-accessible, fluorescence confocal laser scanning microscopy (CLSM)-based technique23,25,29,48 (Figure 5).
Proton conduction environment is not the same across ionomer thin films- Interfacial effects propagate.
We developed a fluorescence confocal laser scanning microscopy (CLSM)-based strategy23,25,29,48 that can probe the distribution of mobility, ion conduction, and other properties across ionomer samples. Using CLSM, we were the first to reveal that ionic conduction across ionomer thin films varies along the depth of the films and is highly interface-dependent.23,25,29,48 To probe the depth-specific proton conduction properties across ionomer thin films and membranes, we incorporated HPTS dye into Nafion thin films and membranes and then placed them under a confocal microscope inside a humidity-controlled chamber. We took multiple xy-plane images at different depth within dry/hydrated ionomer samples. Subsequently, these xy-plane mages were z-stacked to obtain a depth profile image representing the fluorescence response of HPTS along the thickness of the ionomer samples (Id/Ip profile, Figure 5a,b). This Id/Ip profile revealed the distribution of proton-conduction environment across hydrated ionomer thin films/membranes.
When we took CLSM images, we observed distinctly different proton conduction behavior (Id/Ip) across bulk, free-standing Nafion membrane (35 μm thick) and sub-micron thick Nafion films25 (Figure 5b). In bulk Nafion membrane, proton conduction environment (assessed from Id/Ip profile) was almost uniform across the membrane. However, proton conduction of Nafion thin films (on glass substrates) was extremely weak over a broad region next to the substrate interface, then gradually increased as we approached the air interface (Figure 5b).25 The overall Id/Ip profile was found to be thickness- and humidity-dependent. However, humidification could not make the near-substrate region more favorable for proton conduction (Figure 5b, z/d ~0). It was also interesting to see that low-proton-conducting region propagated up to about half of the Nafion films starting from the substrate interface (studied 68–1000 nm thick Nafion films).
NR measurements indicated water accumulation near the substrate interface of sub-μm thick ionomer73,74,75 films; while our CLSM images suggested that ionomer chains and these water molecules residing near the substrate interface do not conduct protons efficiently.25 The NR-CLSM observations corroborate with the surface-parallel alignment of Nafion backbones next to substrate60 compelling their side-chain -SO3H to face and pin to the substrate (Figure 5c). Such pinned ionomer chains should have lower segmental mobility. Also, the water molecules H-bonded to this substrate and substrate-pinned ionomer chains will have their rotational mobility compromised. When we looked at CCVJ-stained and hydrated Nafion films under CLSM, we identified a stiffened region next to the substrate within these Nafion films.25 Moreover, the width of the antiplasticized region near the substrate interface was comparable to the width of the low-Id/Ip region of a film. This demonstrated the critical role played by interfacial processes and water-ionomer mobility on thin-film ionic conductivity.
Having said that, the water-rich layers, identified by NR, are much thinner (~10 nm) than the low-conducting, low-mobility regions (about half of film thickness) captured by CLSM. This suggested that the substrate interface alone likely does not control the mobility and conductivity. We observed hump-like mobility distribution curves (CLSM) indicating the lowest mobility in the film’s middle. This could be attributed to polymer chain or chain segment crowding in this region.67 Apparently, it made sense because the mid-region of Nafion films on SiO2 was more polymer-rich than the next-to-substrate region (NR).77 Others reported maximum chain entanglement density in the middle of the films.126 Dense packing of entangled polymer chains can lower the chain mobility and stiffen the mid-region of the films. Lastly, if some chains are pinned to the substrate at one end, and extend across the film, their mobility may be controlled by substrate.127 Together these facts (Figure 5c-right) explain the origin of broad, low-conducting, low-mobility regions in Nafion films. In contrast, the air interface, free from these constraints, showed better proton conduction.
Overall, this CLSM-based strategy made a groundbreaking advancement in our understanding of ionomer thin films and ionomer-substrate interfaces. Previously, we had no other choice but to rely on an average value of proton conductivity (σ) for an entire ionomer sample, measured using electrochemical impedance spectroscopy (EIS). Now, we can reveal the depth-specific proton conduction behavior and tell how far the interfacial effects propagate inside very thin films. After demonstrating the proof-of-concept, we extended this CLSM-based strategy to understand several ionomeric systems.29,23,48 Especially, we used CSLM to distinguish the depth-specific proton-conduction environment across Nafion films on unmodified and engineered substrates.29 We also located a specific feature in a film of a biomimetic ionomer and assessed proton conduction across the feature.23
ENGINEER ionomer-substrate interface.
Can we manipulate the distribution of ion conduction environment?
Realizing that interfacial interactions are detrimental to water-polymer mobility24,25,54,69,75,128 and proton conduction,24,25 leading to poor proton conduction over a broad region near the substrate (Figure 5b), we started to think if we can manipulate the interfacial makeup in a way to improve thin-film proton conductivity and alleviate ion transport limitations. Interfacial engineering is crucial for ionomer-catalyst binder layers in PEMFC cathodes, as surface-parallel ionomer chains can cover catalyst particles, block ORR active sites, cause gas (O2) transport limitation, and reduce PEMFC performance.32,48,117,129,130
To date, various approaches have been employed to engineer model substrates and catalysts to alter their physical and chemical properties. Apart from altering the structure and chemistry of catalysts,131,132,133 interfacial restructuring of model substrates has been grabbing attention lately. For example, substrate hydrophilicity132,134,135,136 or zeta potential132 was altered, substrate interface was doped with certain atoms137,138,139 or modified via covalent/electrostatic immobilization of certain molecules, like, block copolymers, ionic liquids (ILs),136,140,141,142,143 IL-modified block copolymers,31,144,145 or peptides.32,71,146 Different approaches impact substrates and electrodes differently. For instance, Renner et al.32 modified Pt electrodes with genetically engineered peptides having Pt-binding domains. The -NH2 groups of Pt-bound peptides enabled Nafion adsorption on Pt with altered film morphology and higher Pt-coverage. On the contrary, block copolymers with both -SO3H and IL moieties (SPILBCPs)31 doubled the kinetic performance of MEAs due to reduced coverage of the Pt surface. Snyder et al.30 improved electrocatalyst performance inside pores of the electrodes by embedding catalysts with hydrophobic protic IL. In general, rendering hydrophobicity to surfaces132,134,135,136 or favorably orienting the lamellar structure147,148 may weaken the adsorption of -SO3− anions of Nafion chains onto the substrate.
Our hypothesis was that a porous or brush-like or spider-web-like architecture near the substrate could prevent surface-parallel alignment and anchoring of ionomers and enhance proton conduction. As proof of concept, we adopted a simple yet robust substrate engineering approach. First, we treated the substrate interfaces with (3-aminopropyl)triethoxysilane (APTES), and then deposited sub-μm thick Nafion films on top (Figure 6a).29 Prior endeavors in this field primarily focused on materials development. Our goal was not just to demonstrate a new interface engineering approach, but to delve into underlying mechanisms driving proton conductivity through addressing fundamental, unexplored questions. For instance, existing literature lacks interface- and depth-specific information on proton conduction which we explored using our previously established CLSM protocols.25 This unique interface-specific information was complemented further by looking into the physical, chemical and mechanical change happening at the substrate interface.
Our investigation uncovered that APTES modification reduced the hydrophilicity of the SiO2 substrate and boosted both in-plane (σIP) and out-of-plane (σOP) proton conductivity of Nafion thin films (Figure 6b).29 For example, in Nafion films with thickness (~60 nm) closer to catalyst binder ionomer layers in PEMFCs, silane induced 2-times improvement in σIP and at least 10-times improvement in σOP (Figure 6b). APTES itself had negligible conductivity, thus had negligible contribution to the total conductivity of the Nafion-silane ensemble. Most importantly, APTES-based substrate modification narrowed down the low-conductivity region next-to-substrate and an overall enhancement in protonic conduction behavior across the entire Nafion films on silane, as revealed by Id/IP profile from CLSM imaging (Figure 6c).29
Interestingly, silane did not alter the water uptake by the Nafion films, but significantly altered the phase segregation, ionomer chain packing, pinning, orientation, and distribution of Nafion chains.29 The loss of correlation in Nafion films deposited on silane-modified substrates (GISAXS, Figure 6d) manifested an induced disorder in lamella and/or a randomization of ionomer chains in all directions.29 Moreover, SEM-EDX-based elemental mapping showed that the APTES layer over the substrate led to a reduced population of Nafion chains next to the substrate (Figure 6e). For example, %F, %S near substrate interface of ~150 nm thick Nafion films: 46.3%, 0.45% (no silane); 23.10%, 0.21% (with silane).29 The APTES layer also altered ionomer chain orientation in the films overall and led to a more isotropic (randomized) chain structure. The randomization was such that it favored proton conduction more in thin Nafion films on APTES. Last but not least, silanization reduced the elastic modulus of Nafion films (Figure 6f) indicating reduced Nafion-substrate interactions and reduced chain pinning to substrate upon silanization, making Nafion films on silane less stiff than that on unmodified substrates.29
Overall, this surface engineering approach29 offered a promising pathway to alter the physical-chemical makeup of the ionomer-substrate interface, negate interfacial lamella and chain pinning, and improve interfacial as well as across-the-film proton conductivity of Nafion. It opened new avenues to overcome the ion-transport limitation. Especially, the study provided deep mechanistic insights into interfacial phenomena and the propagation of their effects, distinguishing it as a unique contribution to the field. Combining findings from EIS, CLSM, GISAXS, SEM-EDX, ellipsometry, and CR-AFM created a comprehensive platform to understand interfacial processes in ionomer-substrate and ionomer-catalyst systems, relevant to diverse electrochemical technologies like fuel cells, electrolyzers, and batteries. Currently, our focus lies in comprehending the impact of different functionalization on interfacial ion conductivity, aiming to further optimize proton conduction in thin film systems (reported in future communications).
DESIGN new ionomers to improve thin-film and interfacial proton conductivity.
Based on our current understanding, it is time to realize that for the catalyst binder layer, we should prioritize using the ionomers designed keeping in mind the specific issues associated with ionomer thin films over those originally intended for membranes. This is because the design needs for ionomers for catalyst binder layers are distinctly different from those for bulk membranes. We revealed that interfacial effects, poor phase separation, and small, scattered, poorly connected ionic domains24,70,95 are the major issues adversely affecting the proton conductivity of ionomer thin films mimicking catalyst binder layers. Our observations are in complete agreement with what DOE-HFTO’s 2023 annual merit review5 reported. As per the report, by advancing the ion and gas transport pathways in electrode design, up to ~50% higher power density can be achieved.5,149 The report also suggests pathways to reduce PEMFC stack costs. By increasing power density and reducing the loading of platinum group metal (PGM) catalysts in electrodes, PEMFC system cost can be reduced by 20%.5 The connection between proton conductivity, power density and cost is: high proton conductivity would lead to high ORR efficiency and high power density; and achieving high power output from relatively smaller PEMFC stacks would reduce stack manufacturing costs.11
Therefore, any ionomer that can alleviate proton transport limitation while minimizing cost and environmental concerns, would be ideal as ionomer binders for PEMFCs. The high-cost (Nafion: $500/kg)150 and environmental concerns of fluorocarbon-based ionomers have made the research community shift toward hydrocarbon-based ionomers. At the current context, with raised concerns about perfluorinated compounds (PFAS), this transition is even more important. However, as discussed earlier, traditional fluorocarbon (Nafion)- and hydrocarbon-based ionomers (sPSf, sPEEK), designed for membranes and conducting protons efficiently in bulk membranes, perform poorly in thin films and cathode catalyst layers or MEAs. For instance, Nafion thin films (9 mS/cm) showed over an order of magnitude higher proton conductivity than sPSf films (0.2 mS/cm).48 Binder-phase/MEA-level studies of traditional hydrocarbon-based ionomers (Figure 7, left panel, Table 3) also supported severe diffusion limitations18,19 and lower power densities.20,21,22 As can be seen in Table 3, at comparable testing conditions, the power densities of MEAs made of typical hydrocarbon-based ionomers was roughly an order of magnitude lower than fluorocarbon-based ones at 0.7 V. While fluorocarbon-based MEAs exhibit a power density around 1 W/cm2 at 0.7 V (Table 3),8,151 the desired power density for fuel cell vehicles is 2.1–3.2 W/cm2 at 0.7–0.8 V (equivalent to a current density of 3–4 A/cm2 at 0.7–0.8 V).9 Catalyst design has received much attention and efforts,10,26,27,28 but ionomer design for catalyst binder layers has long been overlooked. In fact, the tendency has been to employ the same ionomers as catalyst binders that work well for membranes. This is where we contributed over the last few years.
Figure 7.

Chemical structures of hydrocarbon-based ionomer classes studied in thin films or at MEA level. Chemical structures redrawn with permission from refs: sPEEK: sulfonated poly(ether ether ketone);98 sPE/sPSf/sPSU/sPAES/BPS: derivatives of sulfonated polysulfone or poly(arylene ether sulfone);48,152,153,154 sPPP: sulfophenylated poly(phenylene);155 Pemion: derivative of sulfophenylated poly(phenylene);105 sPPB: sulfophenylated poly(phenylene) biphenyl22 Nexar: sulfonated styrene-based pentablock terpolymer;156 p(DA/AADDA): polyethylene with acrylamide and amidoalkylcarboxylic acid side chains;157 p(DDA/AA): polyethylene acrylamide and carboxylic acid side chains;158 sPI: derivatives of sulfonated polyimide;159 polypeptide;160 PVCa-b-PSt: poly(vinyl catechol)-block-poly(styrene);161 LS: lignin sulfonic acid;69 calix-2: sulfonated calix[4]arene-sulfonated biphenyl;23 PS-calix: polystyrene backbone with sulfonated calix[4]arene pendants.48 Copyrights 2013, 2015, 2016, 2018, 2022, American Chemical Society; Copyright 2023, Cell Press; Copyright 2020, Frontiers; Copyrights 2008, 2015, 2021 Elsevier; Copyright 2001, 2018 Wiley; Copyrights 2007, 2019, 2020, The Electrochemical Society; Copyright 2021, Royal Society of Chemistry.
The earlier limited, thin-film focused ionomer design efforts relied majorly on creating extreme lamellar structures using polyimide,159,172,173,178 polypeptide,160,176 and polyethylene157,158,175 derivatives (Table 4, Figure 7, left panel highlighted blue). The fundamental idea behind these efforts was to achieve an ordered layered structure to enable transport better than tortuous pathways. Creating highly preferential alignment of ionomer chains (lamella) gave rise to enhanced in-plane proton conductivity, but at the same time, made proton conduction highly anisotropic.157,158,176 This is expected as the surface-parallel lamella in Nafion thin films does the same (e.g., s: 3.3 mS/cm (IP) vs. 3×10−6 mS/cm (OP) for ~20 nm thick Nafion film, Table 4) and we showed that avoiding or disrupting near-substrate lamella may improve both in-plane and out-of-plane proton conductivity (Figure 6b).
Table 4.
Proton conductivity of reported ionomers in thin films.
| Ionomer | IEC | Substrate | Annealing condition | Film thickness (nm) | %RH | Temperature (°C) | Proton conductivity (mS/cm)* | Ref |
|---|---|---|---|---|---|---|---|---|
| Polyimide backbone | ||||||||
| Sulfonated polyimide (linear) | 2.89–3.11 | SiO2 | Unannealed | 500 nm | 95 | 25 | 158 | 159 |
| Sulfonated polyimide (bent) | 2.72–2.78 | SiO2 | Unannealed | 500 nm | 95 | 25 | 63 | 159 |
| Sulfonated polyimide (oriented lamella) | 2.9 | SiO2 | Unannealed | 500 nm | 95 | 25 | 150 | 172 |
| Sulfonated polyimide (disoriented lamella) | 2.9 | SiO2 | Unannealed | 500 nm | 95 | 25 | 30 | 172 |
| Sulfonated polyimide-block-hydrophobic polyimide | 2.69 | SiO2 | Unannealed | 500 nm | 95 | 25 | 32 | 173 |
| Polyethylene backbone | ||||||||
| Acrylamide and amidoalkylcarboxylic acid side chains, p(DA/AADDA) | n.a. | Hydrophobic glass | Unannealed | 900 nm | 98 | 60 | 1.7×10−3
(IP) 4×10−6 (OP) |
157 |
| Acrylamide and carboxylic acid side chains, p(DDA/AA) | n.a. | Hydrophobic glass | Unannealed | 60 nm | 98 | 60 | 51
(IP) 2×10−11 (OP) |
158 |
| Acrylamide and vinylphosphonic acid side chains | n.a. | Hydrophobic silicon | Unannealed | - | 98 | 60 | 32 | 174 |
| Folded backbone with precisely positioned sulfonic acid side chain | n.a. | None (Free-standing film) | Annealed | 200,000 nm | 100 | 40 | 100 | 175 |
| Polypeptide backbone | ||||||||
| Poly(aspartic acid)/sodium aspartate | n.a. | MgO | Unannealed | 60 nm | 70 | 25 | 3.4 | 160 |
| Poly(aspartic acid)/sodium aspartate | glass | Unannealed | 60 nm | 50 | 25 | 2.7×10−3
(IP) 3.4×10−6 (OP) |
176 | |
| Polystyrene backbone | ||||||||
| Poly(vinyl catechol)-poly(styrene) block copolymer-Ag np, PVCa-b-St | n.a. | quartz | unannealed | 200 nm | 95 | n.a. | 0.1 | 161 |
| MOF | ||||||||
| Cu-TCPP nanosheet | n.a. | SiO2 | Unannealed | 350 nm | 40 | 25 | 3.2×10−5 | 177 |
| 90 | 6.2×10−2 | |||||||
| COF | ||||||||
| Nafion | 1 | SiO2 | Unannealed | 25,000 nm | 90 | 30 | 7 | |
| SDT-COF-Nafion | 1.70 (COF) | 10.5 | ||||||
| Our Works | ||||||||
| LS | 1.6 | SiO2 (thermal oxide | Annealed | 25 nm | 85 | 25 | 4 | 69 |
| 165 nm | 14 | |||||||
| Calix-2 | 3.9 | SiO2 (thermal oxide) | Unannealed | 20 nm | 83 | 25 | 22.57
(IP) 1×10−5 (OP) |
23 |
| 100 nm | 65.5 | |||||||
| PS-calix | 3.85 | SiO2 (thermal oxide) | Unannealed | 15–20 nm | 85 | 25 | 41.1 | 48 |
| 160 nm | 65.4 | |||||||
| sPSf | 1.3 | SiO2 (thermal oxide) | Unannealed | 15–20 nm | 85 | 25 | 0.01 | 48 |
| 160 nm | 0.2 | |||||||
| Nafion | 0.99 | SiO2 (thermal oxide) | Unannealed | 15–20 nm | 83 | 25 | 3.3 (IP) 3 ×10−6 (OP) |
48 |
| 100 nm | 8.3 | 23 | ||||||
| 160 nm | 9 | 48 | ||||||
| Nafion | 0.99 | SiO2 (thermal oxide) | Annealed | 25 nm | 85 | 25 | 0.13 | 69 |
| 165 nm | 1 | |||||||
Unless otherwise stated, proton conductivities are measured in-plane direction.
The terms “IP” and “OP” represent proton conductivity at in-plane and out-of-plane directions.
Our synthetic ionomer design approaches, on the contrary, concentrated more on gaining control over ionic domain size and connectivity and creating multimodal proton hopping pathways. Our ionomer design efforts so far thus can be classified into two categories (Figure 7, right panel, highlighted green): (i) Nature-derived ionomers, and (ii) Nature-inspired ionomers. The nature-derived approach69 leveraged plant polymer lignin as precursor yielding low-cost, sustainable, PFAS-free ionomers with high thin-film proton conductivity. In the nature-inspired approach,23,48 we got inspired by biological ion channels and brought their capabilities into the design of synthetic proton-conducting ionomers which showed proton conductivity superior to Nafion in thin films. Here, we summarily discuss the outcome of these efforts.
Nature-derived ionomers.
Lignin-based ionomers conduct protons more efficiently than Nafion in thin films:
Traditional hydrocarbon-based ionomers, like sPEEK or sPSf differ from fluorocarbon-based ionomers in several key aspects: they have less flexible backbones with less acidic sulfonic acid groups at side chains (pKa : −1 (-SO3H) in sPEEK vs. −6 (-CF2-SO3H) in Nafion),106,179 less pronounced phase separation,106,179 less free volume,180 low density of protonic sites,105 low protonic mobility,106 and narrow, tortuous, and isolated ion-conducting channels.106,179 Also, most of these linear hydrocarbon ionomers block catalytically active surface sites.18 These features hinder proton conduction and gas transport in thin films.14,16,18,48,102,179 We thus need new ionomer formulations to improve proton conduction in thin films, be cost-effective and environmentally friendly at the same time. This quest motivated us to explore plant cell wall polymer, lignin (Figure 8a).
Figure 8.

(a, b) Features of lignin making it suitable for designing ionomers. (c) Synthetic pathway to design lignin-based ionomer (LS). (d, e) AFM images and (f, g) corresponding roughness profiles of Nafion (left) and LS (right) films. (h) Nyquist plots and (h, inset) proton conductivities of Nafion and LS thin films at 85% RH.69 Figures adapted with permission from ref.69. Copyright 2020 Frontiers.
Lignin has many structural features (Figure 8a,b) which makes it an ideal synthetic precursor of ionomers.69 Lignin is the second most naturally abundant polymer. It is a 3-dimensional hyperbranched polymer that has plenty of polar ether (-O-) linkages and hydroxyl (-OH) groups. Within the network-like structure of lignin, these polar/hydrophilic groups can welcome water needed to generate ion-conducting pathways. We functionalized lignin with -SO3H groups to design lignin-based proton-conducting ionomers (LS, Figure 8c). By controlling lignin-to-sulfonating agent ratio, the ion exchange capacity (IEC) was effectively controlled to achieve lignin sulfonic acid (LS) ionomers which were not water-soluble, unlike the commercial water-soluble lignosulfonate coming from pulp and paper industries. This approach enabled us to design lignin-based practical ionomers69 which will not get washed away while conducting protons in the hydrated state in thin films.
LS formed uniform and smooth films when spin-coated. Also, LS films were less dense than Nafion or sPSf in thin films which agreed with the hollow, network-like structures that facilitated the formation of 3D, connected ion-conduction pathways.69 AFM images showed significantly different morphology with ellipsoidal self-assembled features in LS films (Figure 8d-g). Also, by fitting the ionic domain peaks (GISAXS) of Nafion and LS films in geometric models (core-shell, ellipsoidal, cylindrical), we found that LS films showed much larger ionic domains as compared to Nafion films (e.g., 1.55 nm (Nafion) vs. 7.5 nm (LS)). The observation of larger ionic domains in LS films was in total agreement with the proton conductivity values. LS offered significantly higher proton conductivity than Nafion in thin films (Figure 8h).69 For instance, a ~25 nm thick LS film (thickness similar to ionomer binder layer) showed proton conductivity ~ 4 mS/cm which was more than an order of magnitude higher than a Nafion film with similar thickness (Table 4). The same order of magnitude of proton conductivity improvement was achieved for thicker LS films. Additionally, LS films, unlike Nafion films, did not stiffen upon humidification,69 suggesting more mobility of water-ionomer inside LS films. Thus, the larger ionic domains and higher mobility facilitated increased proton conductivity of LS films. Together, the work paved a new way towards designing lignin-based, low-cost, efficient, sustainable, PFAS-free ionomers capable of circumventing the ion conduction limitation of PEMFC electrodes.
Lignin is not only abundant in forests and agricultural residues but also found as a by-product from pulp and paper industries and cellulosic biorefineries. However, only 1–2% of this lignin is valorized181,182,183, 184,185,186,187 and the rest is either burnt or wasted. Traditionally, lignin’s use in energy materials has mostly circled around creating carbon materials for electrodes.188,189,190,191,192,193,194 The 2023 Billion-Ton Report (BT23)195 from the U.S. Department of Energy (DOE)’s Bioenergy Technologies Office highlights the need to rethink our energy systems to decarbonize the economy, emphasizing the potential of waste feedstocks and biomass. By designing lignin-based, environment-friendly solid polymer electrolytes and advancing the design of clean energy technologies, we can bring innovation in lignin valorization. Such efforts can potentially enhance the economic viability of industries (including biorefineries), and support bioeconomy and energy economy simultaneously. While source-to-source variation and limited understanding of unmodified lignin are often considered as challenges to adopt lignin in energy materials, we are up for embracing these challenges and tackling the issues. We plan to extend our studies to various lignin sources and conduct in-depth molecular-to-nanoscale characterization before materials design, aiming to create an extensive database on lignin-based materials.
Nature-inspired ionomers.
In thin films of traditional ionomers, ionic domain formation is severely sacrificed as ionomers lose mobility and cannot efficiently phase separate. We looked for a workaround with a hypothesis: if we can design ionomers having hollow, cavity-forming repeat units with ion-conducting functionalities, at least molecular-level ion transport should be possible through the built-in, molecular-level pores, even when the ionomers are sitting idle and not segregating for well-formed phases. If, by any chance, these ionomers, having hollow, cavity-forming units, can self-assemble in solution (literature supports196,197,198,199), and retain the assembly in the solid state in a way that stacks the pores, we will be able to achieve both short-range and long-range proton conduction pathways and improve proton conductivity in thin films.
The understanding of traditional ionomers aligns with a generalized thought, i.e., proton conductivity declines as the ionic domains shrink in size. For example, the average size of ionic domains in bulk Nafion membranes is 4 nm, while it shrinks to ~1–2 nm with poor domain connectivity in Nafion thin films. Then we also learned from the literature that there can be a striking difference in water-ion transport mechanism when the size of ionic domains/ion channels transitions from narrow (> 1 nm) to very narrow (< 1 nm).200,201 Biological ion channels are very narrow (< 1 nm), but they can transport water and/or ions very efficiently. For example, Gramicidin A202 has a sub-nm pore diameter (~4 Å), but it transports protons very fast. Explaining the proton-conduction mechanism across such very narrow pores is still a work in progress,203,204,205,206,207,208,209,210,211 but a mechanism that is often put forward is: water in sub-nm sized channels with hydrophobic interiors experience frictionless slip flow212 allowing water to diffuse even faster than bulk water. The underlying principle is: unlike branched, H-bonded, 3D water networks in bulk water, water passing through sub-nm pores or channels is compelled to be 1D forming 1D water wire209,210 where water dipoles are preferentially oriented to facilitate proton hopping.211209,210,211 Also, the mobility-retarding effects of H-bonding are alleviated due to the hydrophobic interior of the pores.
A range of porous materials has been reported with broad range of pore size, including polymers with intrinsic microporosity (PIMs),213 metal-organic framework (MOF),214 covalent organic framework (COF),171,215171 imidazole quartets,216 triazole channels,217 graphene,218,219 cyclic peptide nanotubes,220 carbon nanotubes (CNTs)200,211,221 and electrospun hollow nanofibers.222 A large faction of these materials primarily targeted to study host-guest interactions, sensing, gas adsorption, water purification, separation, and osmotic power-driven energy systems.196,207,223,224,225,226,227,228,229,230 Some targeted to improve proton conductivity (e.g., PIM, MOF, COF), but majorly aimed for bulk membranes.222,231,232 Many of these are crystalline and/or insoluble giving rise to solution/thin-film processability and stability issues.233,234 The innovation lies in the design of ionomers having sub-nm-sized hollow repeat units235 – something the community designing fuel cell/ battery ionomers has not been considering. Summarily, for thin films/catalyst layers, there remains a need for porous solid conductor showing a combination of precise angstrom-scale pores, good processibility,214,236 compatibility with catalyst ink materials,214 and elevated proton conductivity in sub-μm thick films and interfaces - critical yet rarely addressed issue in PEMFCs and other electrochemical devices.69,237 To address these needs, we brought the capabilities of biological ion channels into the design of proton-conducting ionomers to enhance proton conductivity under thin film confinement.
Macrocycles can enable thin-film proton conductivity much higher than Nafion.
To mimic biological ion channels, we leveraged the molecular features of calix[4]arene, a hollow and extremely narrow macrocycle (~ 3 Å). In our first effort in this direction, we designed an ionomer, calix-2 (Figure 9a), having sulfonated calix[4]arene and sulfonated biphenyl repeat units.23 Calix-2 forms uniform thin films which address the processibility issue. In ≤100 nm thick films, in-plane proton conductivity of calix-2 (65.5 mS/cm) was up to 8 times higher than the current benchmark ionomer Nafion at 85%RH (Figure 9b), and over an order of magnitude higher than Nafion at 20–25% RH (Figure 9c). This highlighted the significant improvement in proton conductivity achievable with macrocyclic repeat units. Not only that, but we also saw a significant improvement of both in-plane and out-of-plane proton conductivity when calix-2 was used. For instance, for 20 nm thick unannealed films, the proton conductivities were as follows: Nafion: σIP: 3.3 mS/cm, σOP: 3×10−6 mS/cm vs. calix-2: σIP: 22.6 mS/cm, σOP: 1×10−5 mS/cm (Table 4). The reduced anisotropy in proton conductivity and improved out-of-plane proton conductivity (in addition to in-plane) was uniquely different from extreme lamella-forming ionomers (Table 4).
Proton conduction is better at places where macrocycles are located.
To further validate the role of macrocycles, we synthesized a non-macrocyclic ionomer with only sulfonated biphenyl units (SBP). Calix-2 showed about 5-orders of magnitude higher proton conductivity as compared to this non-macrocyclic variant (SBP). For instance, a 49 nm thick SBP film at 80% RH exhibited proton conductivity of 7 × 10−4 mS/cm, while it was 37 mS/cm for calix-2.23 Additionally, a composite film of SBP and monomeric sulfonated calix[4]arene (Scalixmono) in a 1:0.2 wt ratio showed proton conductivity of 17.5 mS/cm, significantly higher than pure SBP.23 Furthermore, incorporating the photoacid dye HPTS in Nafion-calix-2 composite films demonstrated that proton conduction was stronger at places where macrocycles were located and weaker where Nafion was located (Figure 9d). This array of evidence reinforced the role of hollow macrocyclic cavities in enhancing thin-film proton conductivity.
Macrocycle-based ionomers can generate multi-length scale ion-conduction pathways.
While Nafion thin films appeared almost featureless (Figure 9d), calix-2 ionomers formed ellipsoidal self-assembled structures based on amplitude and 3-dimensional AFM images (Figure 9e). GISAXS showed two ionic domain peaks the d-spacing of which suggested: (i) ionic domains through macrocyclic calix repeat units; (ii) interstitial ionic pathways between two layers of single calix chains. The computed characteristic distances/dimensions from atomistic simulation closely matched with the experimentally measured domain spacing using GISAXS, suggesting that the calix units in these spherical features stacked like buckets (Figure 9f).23 Additionally, during DFT optimization, we observed spontaneous proton transfer from –SO3H groups to H2O molecules within the channels, forming H3O+. Thus, stacking likely facilitated the formation of water wires inside calix channels (Figure 9f). Consequently, proton conduction pathways in calix-2 were likely multi-dimensional: one through the calix cavities, and another along the -SO3H groups on the surface of the calix repeat units.
Calix-2 ionomers did not only exhibit higher proton conductivity over Nafion in thin films and membranes, but also introduced voltage-dependent directionality in ionic current (Figure 9h) within Nafion-calix-2 composite membranes.23 This behavior, due to asymmetric charge distribution in calix units, resembles ionic diodes or voltage-responsive gates, a feature not present in Nafion. This allows for controlled direction and selectivity of ion transport, making these ionomers useful in various electric field-driven energy and separation applications.
Macrocycle-based ionomers can enhance both water and proton transport in thin films.
In another work,48 we synthesized a polystyrene backbone-based ionomer with sulfonated calix[4]arene as pendants (PS-calix, Figure 10a). In films with thicknesses comparable to ionomer-based binder layers (~15–20 nm), PS-calix (IEC 3.85) exhibited conductivity (41 mS/cm) more than an order of magnitude higher than Nafion (3.3 mS/cm) and over 3 orders of magnitude higher than sPSf (0.01 mS/cm) at 85% RH (Figure 10b, Table 4).48 The exceedingly high proton conductivity over Nafion was attributed to an order of magnitude faster water diffusion across PS-calix films, as measured using diffusion-ordered nuclear magnetic resonance spectroscopy (DOSY-NMR): Self-diffusion coefficient of water, Dself, water : 5×10−10 m2/s (Nafion) vs. 7.1×10−9 m2/s (PS-calix, IEC 3.85) at 100% RH in ~300 nm thick films (Figure 10c). Moreover, in some cases, Dself, water in PS-calix films exceeded the reported Dself, water for bulk water (2.3 ×10−9 m2/s).238,239,240,241 This finding aligns with the one by Noy et al.221 on porous carbon nanotubes, which showed that “faster-than-bulk” water transport behavior can be achieved when the CNT diameters are reduced to sub-nm values (Figure 10c). At these dimensions, angstrom-scale conduits can force water molecules to align into a single-file arrangement (1D water wire), allowing frictionless “slip” flow through their hydrophobic cores. Consequently, the faster-than-bulk water transport in thin films likely results from 1D water wires traversing macrocyclic cavities, a feature missing in Nafion. The concurrent observation of high water self-diffusion (Dself, water) and high proton conductivity (σ) in PS-calix indicated that macrocycle-containing ionomers can establish unique and more efficient water and ion-transport pathways, supporting our previous findings for calix-2.23
Macrocycle-based ionomers can minimize substrate pinning and boost thin-film proton conduction behavior.
Using CLSM and photoacid dye HPTS, we demonstrated that proton conduction (Id/Ip) at the substrate interface and across the film significantly improved when Nafion was replaced by PS-calix (Figure 10d). This is a unique observation as Nafion, unlike PS-calix showed a weaker proton conduction immediate next to the substrate interface (also shown in Figure 6). Later, we also performed elemental mapping at different interfaces of ionomer films using SEM-EDX (Figure 10e). The elemental mapping indicated that %S next to the substrate interface in PS-calix films was less than that in Nafion films. Together the observations using CLSM and SEM-EDX suggested that PS-calix chains were likely oriented in a manner reducing -SO3H groups next to the substrate interface (i.e., less %S next to the substrate as compared to Nafion, Figure 10e). Lower -SO3H accumulation can reduce substrate pinning of ionomer chains, weaken substrate-induced confinement, and thus enhance proton conduction at the substrate interface (Figure 10d) as well as across the entire PS-calix films (Figure 10b,d) as we observed.
Macrocycle-based ionomers can address both ion- and gas-transport limitations.
We noted a similar enhancement in proton conductivity when PS-calix was interfaced with Pt nanoparticles, highlighting its potential for PEMFC catalyst inks. In mixed films with Pt nanoparticles, PS-calix exhibited proton conductivity an order of magnitude higher than Nafion-Pt films (Figure 10f). On another note, strong adsorption of ionomer chains on catalyst particles can obstruct active sites, leading to O2 transport resistance in PEMFC cathodes.58,117 We observed that PS-calix masked the Pt nanoparticles less than Nafion (Figure 10g). By keeping more electrochemically active surface area of catalysts exposed, PS-calix can potentially reduce gas transport limitation while also alleviating ion transport limitation. These improvements in both ion- and gas transport properties at nano thin catalyst interfaces using PS-calix opened new pathways for advancing ionomer design for PEMFC electrodes. By effectively channeling water and ions through appropriately sized constrictions, these PFAS-free ionomers could serve as highly efficient catalyst binder ionomer layers for fuel cells, electrolyzers, batteries, and various other sustainable energy technologies.
Broader impact, outlook, and conclusions.
In this feature article, we highlighted our contribution to advancing the field of ionomers in sub-μm thick films, a relatively less explored area, but highly relevant to electrodes of clean energy technologies. Our focus was on proton-conducting ionomers relevant to PEMCs. We developed an extensive platform to deeply understand interfacial processes and find the routes to ion transport limitations in thin films of traditional ionomers. The gained insights guided the hypothesis of engineering ionomer-catalyst interface to manipulate interfacial chemical and orientational makeup. We showed that modifying interfacial chemistry can significantly alleviate the confining effects on ionomer thin films and water molecules.29 Finally, ionomers are rarely designed considering the factors impeding proton conduction in nano-thin ionomer binder layers. We pioneered the design of novel fluorine-free ionomers23,48,69 with the capability to address ion and gas transport limitations, key challenges of PEMFCs, while addressing sustainability and environmental concerns. This much-needed synthetic improvement on ionomer can transform PEMFCs and beyond.
Looking ahead, the “unraveling-engineering” efforts set the stage for exploring more complex interfacial systems in future. The systems could be ionomers at real catalyst interfaces for batteries and PEMFCs to address ion transport resistance. Also, the designed tools and strategies could be vital to understand the polymer-microbe interface to deal with antibiotic resistance, another area where we actively work on.182,242,243 We will concurrently pursue meticulous surface nanostructuring to engineer the ionomer-catalyst interface, aiming to optimize proton and gas transport efficiency for enhanced fuel cell performance. Last but not least, while the development of novel fluorine-free ionomers surpassing traditional Nafion in performance represents a significant achievement, further research into environmentally benign synthetic pathways for these materials, understanding the stability or durability of newly designed ionomeric materials, integrating them in MEAs, and studying their performance under PEMFC-relevant conditions will further demonstrate their utility in practical device settings. Additionally, extending the applications of these new ionomers to other electrochemical and blue energy harvesting systems is a prudent and strategic progression of our work toward a sustainable, low-carbon energy future.
Acknowledgements.
S.K.D. acknowledges the supports from the National Science Foundation (NSF) CAREER Award (NSF-DMR # 1750040), NSF-CBET #2310185 (Electrochemical Systems), and the U.S. Department of Energy (DOE), Office of Science, Basic Energy Sciences (BES) Early Career Award (#DE-SC0020336). K.A.C. thanks the Fulbright Scholars Program and the University of Nebraska Collaboration Initiative Grant for their support. R.K. thanks National Overseas Scholarship (India) for partial support. Part of this research (DSC, TGA, RSAXS, SE, XPS, nanofabrication) was performed in the Nebraska Nanoscale Facility: National Nanotechnology Coordinated Infrastructure and the Nebraska Center for Materials and Nanoscience, which are supported by the National Science Foundation under Award NNCI-1542182, ECCS: 2025298 and the Nebraska Research Initiative. The CLSM images were taken at the Morrison Microscopy Research Core Facility of the Nebraska Center for Biotechnology, which is partially funded by the Nebraska Center for Integrated Biomolecular Communication COBRE grant (P20 GM113126 and NIGMS). We acknowledge the UNL Molecular Analysis and Characterization (MAC) Facility for NMR, and GPC works and the Nebraska Center for Integrated Biomolecular Communication (NCIBC). A helium recovery system supporting the NMR spectrometers was purchased with support from the NCIBC Systems Biology Core (NIH NIGMS P20 GM 113126). The authors also thank Nano-Engineering Research Core Facility (NERCF) at UNL for AFM studies of ionomeric materials.
Footnotes
Conflicts of interest.
The authors declare no conflict of interest.
Data availability statement.
This feature article did not include any primary research result, software, or code, and no new data were generated or analyzed.
Notes and references.
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