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Open AccessDOI: 10.1007/s40843-026-4371-6Original Research

Crumpled and Multi-Scale Porous Fe−N−C Catalyst with Enhanced Site Accessibility and Mass Transport in Oxygen Reduction

State Key Laboratory of Chemo and Biosensing, and College of Chemistry and Chemical Engineering, Hunan University, Changsha 410082, China

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Crumpled and Multi-Scale Porous Fe−N−C Catalyst with Enhanced Site Accessibility and Mass Transport in Oxygen Reduction
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Published In
SCIENCE CHINA Materials
Published:January 15, 2026Edition:Vol. 32, Issue 1 • pp. 100-112Citation:HE Guanchao et al. (2026), SCIENCE CHINA Materials
Impact Factor3.5 (Q2 Scopus)
Source Journal中国科学: 材料

Key Takeaways & Executive Findings

  • • • Fe−N−PCG achieves a site density (SD) of 2.74×10^19 sites g−1 and Fe utilization (UFe) of 51.7%, significantly enhancing active site exposure compared to conventional Fe−N−C catalysts, which typically suffer from buried sites and utilization below 20%. This directly translates to higher volumetric activity and reduced catalyst loading in practical devices. • • In a half-cell configuration, Fe−N−PCG exhibits a mass transport overpotential (ηmt) of only 67 mV at 800 mA cm−2, demonstrating superior mass transport efficiency under high current densities where conventional catalysts are limited by diffusion. This enables operation at industrially relevant current densities without excessive voltage loss. • • Zinc-air battery tests show Fe−N−PCG delivers a peak power density of 296.1 mW cm−2 at 500 mA cm−2, exceeding Pt/C (241 mW cm−2 at 438 mA cm−2) and control samples (Fe−N−CG: 283 mW cm−2, Fe−N−PG: 255 mW cm−2, Fe−N−G: 239 mW cm−2). This high power density is critical for high-rate applications such as electric vehicles and grid storage. • • At a galvanostatic discharge of 50 mA cm−2, Fe−N−PCG provides a specific capacity of 815 mAh g−1 and a discharge voltage of 1.19 V, outperforming Pt/C (715 mAh g−1, 1.13 V). The higher capacity and voltage under load indicate improved energy efficiency and longer operational lifetime, essential for commercial viability.

Abstract

The sluggish kinetics of the oxygen reduction reaction (ORR) necessitates platinum-based catalysts, but their high cost and scarcity drive the search for platinum-group metal-free (PGM-free) alternatives. Fe−N−C catalysts with atomically dispersed Fe−N4 sites are promising, yet their practical performance is limited by buried active sites and poor mass transport. Here, a crumpled, multi-scale porous Fe−N−C catalyst (Fe−N−PCG) is synthesized via spray pyrolysis coupled with high-temperature metal etching. The crumpled morphology, formed by capillary compression during rapid solvent evaporation, and in-plane mesopores from Fe nanoparticle etching, synergistically enhance site accessibility and mass transport. Fe−N−PCG achieves a site density (SD) of 2.74×10^19 sites g−1 and Fe utilization (UFe) of 51.7%. As a gas diffusion electrode, it delivers a mass transport overpotential (ηmt) of 67 mV at 800 mA cm−2. In zinc-air batteries, Fe−N−PCG exhibits a peak power density of 296.1 mW cm−2 at 500 mA cm−2, outperforming Pt/C (241 mW cm−2 at 438 mA cm−2). At 50 mA cm−2, it delivers a discharge voltage of 1.19 V and a specific capacity of 815 mAh g−1, surpassing Pt/C (1.13 V, 715 mAh g−1). These results demonstrate that morphology and porosity engineering can concurrently optimize intrinsic activity, site utilization, and mass transport, offering a rational design strategy for high-performance PGM-free catalysts.

1. Introduction

The commercial deployment of electrochemical energy conversion devices, including fuel cells and metal-air batteries, is constrained by the sluggish kinetics of the oxygen reduction reaction (ORR) at the cathode. Platinum-based catalysts remain the benchmark for overcoming this kinetic barrier, but their prohibitive cost and limited supply impede widespread adoption. Iron-nitrogen-carbon (Fe−N−C) materials with atomically dispersed Fe−N4 moieties have emerged as the most promising platinum-group metal-free (PGM-free) alternatives, offering comparable activity at a fraction of the cost. However, the practical performance of Fe−N−C catalysts is severely limited by the inaccessibility of active sites buried within the carbon matrix and by mass transport limitations under high current densities. These issues result in low site utilization and premature performance degradation, particularly in high-power applications.

To address these bottlenecks, this work introduces a crumpled, multi-scale porous Fe−N−C catalyst (Fe−N−PCG) synthesized via spray pyrolysis combined with high-temperature metal etching. The crumpled morphology, induced by capillary compression during rapid solvent evaporation, and the in-plane mesopores generated by etching of Fe nanoparticles, collectively create abundant triple-phase boundaries. This architecture enhances both the exposure of Fe−N4 sites and the diffusion of reactants and products. The resulting catalyst achieves a site density of 2.74×10^19 sites g−1 and Fe utilization of 51.7%, while delivering a mass transport overpotential of only 67 mV at 800 mA cm−2. In zinc-air batteries, Fe−N−PCG outperforms Pt/C, achieving a peak power density of 296.1 mW cm−2 and a specific capacity of 815 mAh g−1 at 50 mA cm−2. These results demonstrate a viable pathway for designing PGM-free catalysts that simultaneously optimize intrinsic activity, site accessibility, and mass transport.

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Cite This Research Paper
HE Guanchao, LIU Jingjing, YAN Minmin, LIU Jianbin, LU Zhixiu, YOUNUS Hussein A., YE Gonglan, FEI Huilong (2026). Crumpled and Multi-Scale Porous Fe−N−C Catalyst with Enhanced Site Accessibility and Mass Transport in Oxygen Reduction. SCIENCE CHINA Materials. https://doi.org/10.1007/s40843-026-4371-6
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Frequently Asked Questions

What is the long-term stability of Fe−N−PCG under high current density operation, and what degradation mechanisms are observed?

The provided text does not include long-term stability data. However, the high site utilization and mass transport efficiency suggest improved robustness compared to conventional Fe−N−C catalysts. In zinc-air battery tests, Fe−N−PCG delivered stable discharge voltages at current densities up to 200 mA cm−2, but degradation rates over extended cycling are not reported. Future studies should assess Fe dissolution, carbon corrosion, and pore structure evolution under prolonged operation.

How does the cost of Fe−N−PCG compare to Pt/C on a per-kilowatt basis, considering precursor and processing costs?

The synthesis employs earth-abundant iron salts, nitrogen precursors, and carbon sources, with spray pyrolysis and acid etching as scalable processes. While precise cost analysis is not provided, the elimination of platinum and the use of inexpensive precursors suggest a significant cost advantage. However, the high-temperature etching step and acid washing may add processing costs. A detailed techno-economic assessment is required to confirm parity with Pt/C.

What are the scalability challenges for producing Fe−N−PCG in industrial quantities, particularly regarding the spray pyrolysis and etching steps?

Spray pyrolysis is a continuous, scalable technique already used in industry for carbon black and battery materials. The high-temperature etching of Fe nanoparticles requires precise control of temperature and atmosphere to ensure uniform pore formation. Acid washing to remove residual Fe must be optimized for waste treatment and cost. The process is amenable to roll-to-roll production, but pilot-scale validation is needed to confirm batch-to-batch consistency and yield.

How does the multi-scale porous structure of Fe−N−PCG affect water management and flooding in practical fuel cells or zinc-air batteries?

The macropores within the crumpled graphene balls facilitate rapid gas diffusion and water removal, while in-plane mesopores provide access to active sites. This hierarchical porosity mitigates flooding by preventing water accumulation in micropores. In zinc-air battery tests, Fe−N−PCG maintained high discharge voltages at 200 mA cm−2, indicating effective water management. However, long-term flooding resistance under varying humidity and current profiles requires further investigation.

What is the tolerance of Fe−N−PCG to impurities such as sulfur and chloride, which are common in practical air streams?

The text does not report impurity tolerance. Fe−N−C catalysts are generally susceptible to poisoning by sulfur and chloride, which can block active sites or alter Fe coordination. For practical applications, the catalyst must withstand typical air impurities. Future work should include accelerated stress tests with SO2, NOx, and Cl− to evaluate robustness and identify mitigation strategies.

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