Numerical performance analysis of solid oxide fuel cell stacks with internal ammonia cracking

被引:11
|
作者
Rizvandi, Omid Babaie [1 ]
Nemati, Arash [1 ]
Nami, Hossein [1 ]
Hendriksen, Peter Vang [1 ]
Frandsen, Henrik Lund [1 ]
机构
[1] Tech Univ Denmark DTU, Dept Energy Convers & Storage, Bldg 310, DK-2800 Lyngby, Denmark
关键词
Solid oxide fuel cell stack; Ammonia-fueled operation; Stack-scale modeling; Ammonia cooling effects; High-temperature gradient; Thermal stresses; MULTIPHYSICS MODEL; DECOMPOSITION; OPERATION; HYDROGEN; ANODE; TOOL;
D O I
10.1016/j.ijhydene.2023.05.321
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Ammonia-fueled operation of solid oxide fuel cells is a promising alternative to their hydrogen-fueled operation. However, high ammonia decomposition rates at elevated operating temperatures of the solid oxide cells lead to a significant temperature drop at the stack inlet, causing increased thermal stresses. A multi-scale model is used in this study to investigate stack performance under direct feed and external pre-cracking of ammonia. Additionally, the effects of co-and counter-flow configurations, gas inflow temperatures, current density, and air flow rate on the stack performance under direct ammonia feed are examined. The simulation results show that for gas inlet temperatures above 750 degrees C, the power densities with direct feed and external cracking of ammonia differ by less than 5%. Moreover, it is indicated that the thermal stresses are lowest for the co-flow case, which decrease with decreasing gas inlet temperature and current density and with increasing air flow. Finally, this study shows that under practically applicable operating conditions, the risk of mechanical failure of the cells under direct ammonia feed operation is small. (c) 2023 The Author(s). Published by Elsevier Ltd on behalf of Hydrogen Energy Publications LLC. This is an open access article under the CC BY license (http://creativecommons.org/ licenses/by/4.0/).
引用
收藏
页码:35723 / 35743
页数:21
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