TY - JOUR
T1 - Numerical investigation of non-uniformity in a tubular solid oxide co-electrolysis stack
T2 - From multi-physics modeling to optimization strategy
AU - Liu, Zerui
AU - Yao, Yue
AU - Shi, Jixin
AU - Wang, Yuqing
AU - Shi, Yixiang
AU - Cai, Ningsheng
AU - Li, Shuang
N1 - Publisher Copyright:
© 2026 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights are reserved, including those for text and data mining, AI training, and similar technologies.
PY - 2026/8/26
Y1 - 2026/8/26
N2 - A 10-cell tubular solid oxide electrolysis cell (SOEC) stack for CO2/H2O co-electrolysis is fabricated and analyzed through a validated three-dimensional multiphysics model. The simulation reveals pronounced intra-cell and inter-cell thermal non-uniformities, encompassing an inlet temperature gradient of 26.70 K/cm and a cell-to-cell thermal standard deviation of 14.89. To mitigate these issues, two novel anode-side blowing strategies, stepped and front blowing, are proposed and evaluated. The stepped blowing configuration reduces the maximum intra-cell temperature gradient by 35.73% and enhances overall electrochemical performance by 21.64% at an operating voltage of 15 V. The front blowing arrangement lowers the inter-cell thermal standard deviation by 54.73% while improving stack performance by 18.83%. As indicated by the above-mentioned results, tailored anode flow management can effectively alleviate thermal imbalances in tubular SOEC stacks, thereby offering a practical and scalable pathway toward more efficient and durable co-electrolysis systems for power-to-X applications.
AB - A 10-cell tubular solid oxide electrolysis cell (SOEC) stack for CO2/H2O co-electrolysis is fabricated and analyzed through a validated three-dimensional multiphysics model. The simulation reveals pronounced intra-cell and inter-cell thermal non-uniformities, encompassing an inlet temperature gradient of 26.70 K/cm and a cell-to-cell thermal standard deviation of 14.89. To mitigate these issues, two novel anode-side blowing strategies, stepped and front blowing, are proposed and evaluated. The stepped blowing configuration reduces the maximum intra-cell temperature gradient by 35.73% and enhances overall electrochemical performance by 21.64% at an operating voltage of 15 V. The front blowing arrangement lowers the inter-cell thermal standard deviation by 54.73% while improving stack performance by 18.83%. As indicated by the above-mentioned results, tailored anode flow management can effectively alleviate thermal imbalances in tubular SOEC stacks, thereby offering a practical and scalable pathway toward more efficient and durable co-electrolysis systems for power-to-X applications.
KW - CO/HO co-electrolysis
KW - Solid oxide electrolysis cell
KW - Stack
KW - Thermal non-uniformity
KW - Three-dimensional multiphysics model
UR - https://www.scopus.com/pages/publications/105046227260
U2 - 10.1016/j.ijhydene.2026.156748
DO - 10.1016/j.ijhydene.2026.156748
M3 - Article
AN - SCOPUS:105046227260
SN - 0360-3199
VL - 263
JO - International Journal of Hydrogen Energy
JF - International Journal of Hydrogen Energy
M1 - 156748
ER -