TY - JOUR
T1 - Optimization of cathode functional layers of solid oxide electrolysis cells
AU - Wang, Tengpeng
AU - Li, Tianpei
AU - Wei, Tao
AU - Hu, Xun
AU - Ye, Zhengmao
AU - Wang, Zhi
AU - Wang, Yi
AU - Zhang, Yanxiang
AU - Buckley, C. E.
AU - Dong, Dehua
N1 - Funding Information:
This work is a part of the projects of the Natural Science Foundation of Shandong Province (ZR2017MEM022). D.D. thanks financial support by the National Natural Science Foundation of China (51872123).
Publisher Copyright:
© 2020 American Chemical Society.
PY - 2020/9/9
Y1 - 2020/9/9
N2 - Sluggish CO2 reduction on the cathodes of solid oxide electrolysis cells greatly affects electrolysis performance. However, there is no study systematically investigating the cathode functional layer (CFL), where the reduction occurs. Cathode supports equipped with fast gas diffusion channels were employed as a platform to investigate the CFL, including porosity, NiO/(Y2O3)0.08Zr0.92O2 (YSZ) ratio, and thickness. The porosity was adjusted by pore former content, and a higher porosity generated a higher electrolysis current density, while the porosity improvement is limited by the fabrication process. The three-dimensional microstructure of the CFL with different NiO/YSZ ratios was reconstructed by distance correlation functions to estimate three-phase boundary density, which can explain the optimal NiO/YSZ weight ratio of 60:40 for CO2 electrolysis. Increasing CFL thickness can provide more active sites until the optimal thickness of 35 μm. Further increasing the thickness results in gas diffusion limitation. Based on the channeled cathode supports, the CFL was optimized according to CO2 electrolysis performance.
AB - Sluggish CO2 reduction on the cathodes of solid oxide electrolysis cells greatly affects electrolysis performance. However, there is no study systematically investigating the cathode functional layer (CFL), where the reduction occurs. Cathode supports equipped with fast gas diffusion channels were employed as a platform to investigate the CFL, including porosity, NiO/(Y2O3)0.08Zr0.92O2 (YSZ) ratio, and thickness. The porosity was adjusted by pore former content, and a higher porosity generated a higher electrolysis current density, while the porosity improvement is limited by the fabrication process. The three-dimensional microstructure of the CFL with different NiO/YSZ ratios was reconstructed by distance correlation functions to estimate three-phase boundary density, which can explain the optimal NiO/YSZ weight ratio of 60:40 for CO2 electrolysis. Increasing CFL thickness can provide more active sites until the optimal thickness of 35 μm. Further increasing the thickness results in gas diffusion limitation. Based on the channeled cathode supports, the CFL was optimized according to CO2 electrolysis performance.
KW - cathode functional layers
KW - COreduction
KW - gas diffusion
KW - solid oxide electrolysis cells
KW - three phase boundary
UR - https://www.scopus.com/pages/publications/85090870591
U2 - 10.1021/acsami.0c11194
DO - 10.1021/acsami.0c11194
M3 - Article
C2 - 32805834
AN - SCOPUS:85090870591
SN - 1944-8244
VL - 12
SP - 40917
EP - 40924
JO - ACS Applied Materials & Interfaces
JF - ACS Applied Materials & Interfaces
IS - 36
ER -