Small angle X-ray scattering study for investigating 3D nanoparticle packing structure of Pt catalyst on Gd-doped CeO₂ supports for fuel cells

Tomoyuki Iwata, Kazuhiko Omote and Katsuyoshi Kakinuma

Summer 2024 Volume 40, No. 2 , 01-11

A 3D real-space structural model for fuel cell catalysis systems, consisting of Pt and Gd-doped CeO₂ nanoparticles, was constructed to match simulated small angle X-ray scattering (SAXS) intensity and observed SAXS intensity using the reverse Monte–Carlo (RMC) method. The observed SAXS patterns were well reproduced by those of the simulations. The SAXS–RMC simulation results indicated that the number of nanometer-sized Pt particles is much smaller than the introduced amount. This suggests that most Pt particles are not uniformly distributed throughout the catalysts. Additionally, the coordination number of Pt particles, calculated from the structural model, tends to decrease as the amount of Pt loaded increases, which is consistent with the transmission electron microscopy (TEM) images. 3D pore size distributions using the obtained structure models were compared with the Barrett–Joyner–Halenda (BJH) analysis results for nitrogen gas adsorption data, and the lower quartiles and medians of the pore diameters were reasonably consistent. The presented SAXS-RMC modeling can evaluate both local arrangement of the constituent primary particles and aggregated mesoscale structure.

Highlights

  • A reverse Monte Carlo (RMC) modeling approach combined with small-angle X-ray scattering (SAXS) can reconstruct realistic three-dimensional nanoparticle arrangements in complex fuel cell catalysts rather than relying solely on two-dimensional microscopy.
  • Analysis indicates that the number of uniformly distributed Pt nanoparticles is substantially lower than the nominal Pt loading, suggesting significant Pt aggregation or non-uniform distribution within the catalyst.
  • The reconstructed 3D models provide quantitative information about Pt coordination, pore size distribution, and mesoscale structure that agrees well with complementary TEM and nitrogen adsorption measurements.

Summary

Understanding the three-dimensional arrangement of catalyst nanoparticles is essential for improving polymer electrolyte fuel cell performance because catalytic activity, gas transport, and durability all depend on particle connectivity and pore structure. Conventional characterization methods typically provide only partial information, making it difficult to visualize the complete catalyst architecture.

A modeling approach based on small-angle X-ray scattering (SAXS) and reverse Monte Carlo (RMC) simulation addresses this challenge by constructing three-dimensional structural models that reproduce experimentally measured scattering patterns. The method incorporates a modified Debye scattering equation that significantly reduces computational cost while maintaining accuracy for large, multicomponent nanoparticle systems containing both platinum catalyst particles and gadolinium-doped ceria (GDC) support particles.

The reconstructed models reveal that the effective number of uniformly dispersed Pt nanoparticles is considerably smaller than expected from the nominal Pt loading. This indicates that much of the platinum is concentrated in localized regions rather than being evenly distributed throughout the catalyst. As Pt loading increases, the average number of Pt particles coordinated with each GDC support particle decreases, leaving more support particles without neighboring Pt. These observations are consistent with transmission electron microscopy while extending the analysis to the entire sample volume rather than selected imaging regions.

The 3D structural models also enable quantitative analysis of pore networks. Calculated pore size distributions closely match values obtained from nitrogen adsorption measurements, particularly for median and lower-quartile pore diameters. Because the models simultaneously describe nanoparticle arrangement and pore morphology, they provide a foundation for evaluating additional properties such as gas diffusion, electrical conductivity, and catalyst accessibility, making the approach valuable for optimizing fuel cell catalyst design.

Frequently asked questions

Small-angle X-ray scattering probes structural features over length scales ranging from individual nanoparticles to larger aggregates without destroying the sample. Unlike microscopy, which examines relatively small regions, SAXS measures the bulk material, providing statistically representative information about particle size, aggregation, and pore structure. When combined with structural modeling, it can reconstruct realistic three-dimensional arrangements of catalyst particles throughout the sample.

SAXS measurements alone provide reciprocal-space scattering data rather than direct real-space structures. Reverse Monte Carlo modeling iteratively adjusts particle positions within a simulated three-dimensional structure until the calculated scattering closely matches the experimental data. This process generates structural models that are consistent with the measured scattering and enables calculation of properties such as coordination numbers and pore size distributions.

The modeling indicates that only a fraction of the nominal platinum loading behaves as uniformly dispersed nanoparticles throughout the catalyst. As platinum loading increases, much of the additional Pt appears to become clustered or localized rather than evenly distributed. This results in fewer GDC particles having neighboring Pt particles despite the higher overall platinum content.

Increasing Pt loading decreases the average coordination number between Pt nanoparticles and GDC support particles. Higher-loading samples contain a greater proportion of support particles with no adjacent Pt nanoparticles, indicating that additional platinum preferentially forms localized concentrations instead of creating a more uniformly connected catalytic network.

The pore network controls how reactant gases reach catalytic sites and how reaction products are removed. Pore size and connectivity directly influence gas transport, catalyst utilization, and overall electrochemical performance. Three-dimensional structural models make it possible to evaluate these pore characteristics alongside nanoparticle distributions within the same framework.

The pore size distributions calculated from the reconstructed three-dimensional models were compared with pore sizes obtained from nitrogen adsorption measurements using the Barrett-Joyner-Halenda (BJH) method. The lower quartiles and median pore diameters showed good agreement between the two approaches, providing confidence that the reconstructed structures realistically represent the catalyst morphology.

Traditional Debye scattering calculations become computationally impractical for large nanoparticle systems because they require evaluating every particle pair. The modified Debye scattering equation reduces this computational burden by treating short-range and long-range particle correlations differently while preserving the accuracy needed to model large, multicomponent catalyst structures. This enables practical simulation of systems containing hundreds of thousands of nanoparticles.

Once a realistic structural model has been reconstructed, it can be used to investigate properties that are difficult to measure directly, including gas diffusivity, electrical conductivity, particle connectivity, and catalyst accessibility. This provides a pathway for correlating nanoscale structure with electrochemical performance and optimizing catalyst formulations for improved efficiency and durability.

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