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Mass Transfer and Activation Dual Modification Strategy for Fuel Electrode Interfaces in Solid Oxide Electrolysis Cells
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Yongkang XIANG1, Zhenfa DING1, Xiaoxin ZHANG1, Wanxin ZHANG1, Yifei SUN1, 2
Journal of the Chinese Ceramic Society | 2025, 53(10) : 2952 - 2962
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Journal of the Chinese Ceramic Society | 2025, 53(10): 2952-2962
• Research Article •
Mass Transfer and Activation Dual Modification Strategy for Fuel Electrode Interfaces in Solid Oxide Electrolysis Cells
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Yongkang XIANG1, Zhenfa DING1, Xiaoxin ZHANG1, Wanxin ZHANG1, Yifei SUN1, 2
Affiliations
  • 1.College of Energy Xiamen University, Xiamen 363102, Fujian, China
  • 2.Fujian Provincial Energy Materials Science and Technology Innovation Laboratory (IKKEM), Xiamen 361005, Fujian, China
  • XIANG Yongkang (1999-), male, Master candidate. E-mail:

About Author:

XIANG Yongkang (1999-), male, Master candidate. E-mail:

Published: 2025-10-20 doi: 10.14062/j.issn.0454-5648.20250217
Outline
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Introduction

Solid oxide electrolysis cells (SOECs) are promising devices that use high-temperature electrolysis to convert H2O and CO2 into valuable fuels like H2 and CO. Compared with conventional electrolysis, SOECs operate at elevated temperatures, which improves efficiency via utilizing industrial waste heat and renewable energy sources. However, CO2 electrolysis faces challenges due to the chemical stability of CO2, requiring a high energy input to break its bonds. NiO-YSZ based fuel electrode-supported SOECs are widely used due to their good electrochemical performance and mechanical strength at a high temperature. Nonetheless, some issues such as reduced electrode conductivity, chemical stability, and interface reaction activity during long-term operation hinder their performance and lifespan. It is thus important for the enhancement of gas transport and catalytic activity to optimize the microstructure and composition of the fuel electrode.

Methods

In this work, a dual modification strategy for microstructure optimization and impregnation modification was proposed to improve SOEC fuel electrode performance for CO2 electrolysis. The electrode microstructure was optimized via introducing starch as a pore former during slurry preparation to adjust the porosity and improve gas diffusion. Half-cells consisting of NiO-YSZ support, NiO-YSZ functional layer, and YSZ electrolyte were fabricated by tape casting and sintered at 1350 ℃. In addition, Ce0.8Gd0.15Ni0.05O2 (CGN) was synthesized by a sol-gel method and impregnated into the porous fuel electrode. After impregnation, samples were reduced in hydrogen to produce Ni nanoparticles dispersed on the Ce-based matrix. The microstructure was characterized by scanning electron microscopy (SEM) and X-ray diffraction (XRD), while the oxygen vacancies and active sites were determined by X-ray photoelectron spectroscopy (XPS), electron paramagnetic resonance (EPR), and carbon dioxide temperature programmed desorption (CO2-TPD). The electrochemical performance was evaluated by impedance spectroscopy and current-voltage measurements.

Results and Discussion

The introduction of starch effectively increases the electrode porosity, thus reducing mass transfer polarization resistance and enhancing gas transport. The results of electrochemical tests demonstrate that the optimized electrode has a current density of 0.64 A·cm-2 at 750 ℃ and 1.6 V under CO2 electrolysis atmosphere. The impregnation of CGN precursor leads to the uniform dispersion of Ni nanoparticles and increases oxygen vacancy concentration. These modifications significantly improves catalytic activity toward CO2 reduction, and the electrolysis current density is increased by 58% and 64% at 1.1 V and 1.6 V, respectively. The impedance data indicate a marked decrease in polarization resistance. The long-term stability tests over 100 hours show a stable electrochemical performance, indicating that the combined structural and compositional modifications effectively enhance electrode durability and activity.

Conclusions

The dual modification approach integrating microstructural optimization and CGN impregnation significantly enhanced SOEC fuel electrode performance in CO2 electrolysis. Increased porosity improved gas transport, while Ni catalyst modification boosted catalytic activity and oxygen ion transport. This strategy could provide a practical and cost-effective method to improve SOEC durability and efficiency without using expensive noble metals. The findings could offer a valuable guidance for the development of next-generation high-performance SOEC systems for carbon-neutral energy applications.

solid oxide electrolysis cell  /  carbon dioxide electrolysis  /  microstructure optimization  /  fuel electrode modification
项永康, 丁镇发, 张肖鑫, 张婉馨, 孙毅飞. 固体氧化物电解池燃料极表界面的传质/活化双改性策略. 硅酸盐学报, 2025 , 53 (10) : 2952 -2962 . DOI: 10.14062/j.issn.0454-5648.20250217
Yongkang XIANG, Zhenfa DING, Xiaoxin ZHANG, Wanxin ZHANG, Yifei SUN. Mass Transfer and Activation Dual Modification Strategy for Fuel Electrode Interfaces in Solid Oxide Electrolysis Cells[J]. Journal of the Chinese Ceramic Society, 2025 , 53 (10) : 2952 -2962 . DOI: 10.14062/j.issn.0454-5648.20250217
Year 2025 volume 53 Issue 10
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3
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Article Info
doi: 10.14062/j.issn.0454-5648.20250217
  • Receive Date:2025-03-27
  • Online Date:2026-10-21
  • Published:2025-10-20
Article Data
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History
  • Received:2025-03-27
  • Revised:2025-04-24
Funding
Affiliations
    1.College of Energy Xiamen University, Xiamen 363102, Fujian, China
    2.Fujian Provincial Energy Materials Science and Technology Innovation Laboratory (IKKEM), Xiamen 361005, Fujian, China

Corresponding:

SUN Yifei (1987-), male, Ph.D, Associate Professor. E-mail:
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表12种不同金属材料的力学参数
科
Family
属数
Number of
genus
种数
Number of
species
占总种数比例
Percentage of
total species (%)
属
Genus
种数
Number of
species
占总种数比例
Percentage of total
species (%)
鹅膏菌科Amanitaceae 2 11 5.26 鹅膏菌属 Amanita 10 4.78
小菇科 Mycenaceae 2 12 5.74 丝盖伞属 Inocybe 5 2.39
多孔菌科 Polyporaceae 8 14 6.70 蜡蘑属 Laccaria 5 2.39
红菇科 Russulaceae 3 23 11.00 小皮伞属 Marasmius 6 2.87
小菇属 Mycena 11 5.26
光柄菇属 Pluteus 5 2.39
红菇属 Russula 17 8.13
栓菌属 Trametes 5 2.39
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