Optimization of the electrode-supported tubular solid oxide cells for application on fuel cell and steam electrolysis

被引:25
|
作者
Shao, Le [1 ]
Wang, Shaorong [1 ]
Qian, Jiqin [1 ]
Ye, Xiaofeng [1 ]
Wen, Tinglian [1 ]
机构
[1] Chinese Acad Sci, Shanghai Inst Ceram, CAS Key Lab Mat Energy Convers, Shanghai 200050, Peoples R China
基金
中国国家自然科学基金;
关键词
Tubular solid oxide cells; Steam electrolysis; Gas diffusion resistance; Polarization resistance; TEMPERATURE WATER ELECTROLYSIS; HYDROGEN-PRODUCTION; PERFORMANCE; DEGRADATION; ANODE;
D O I
10.1016/j.ijhydene.2012.12.144
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
Hydrogen electrode-supported tubular solid oxide cells (SOCs) were fabricated by dip-coating and co-sintering method. The electrochemical properties of tubular SOCs were investigated both in fuel cell and electrolysis modes. Ni-YSZ was employed as hydrogen electrode support. The pore ratio of Ni-YSZ support strongly affected the performance of tubular SOCs, especially in steam electrolysis mode. The pore ratio was adjusted by the content of pore-former in support slurry. The results showed that 3 wt.% pore former content is the proper value to produce high performance both in fuel cell and electrolysis modes. In fuel cell mode, the maximum power density reached 743.1 mW cm(-2) with H-2 (105 sccm) and O-2 (70 sccm) as working gases at 850 degrees C. In electrolysis mode, as the electrolysis voltage was 1.3 V, the electrolysis current density reached 425 mA cm(-2) with H-2 (35 sccm) and N-2 (70 sccm) adsorbed 47% steam as working gases in hydrogen electrode at 850 degrees C. The stability of tubular SOCs was related to the ratio of NiO/YSZ in the support. The sample with NiO/YSZ = 60/40 shows a better performance than the sample with NiO/YSZ = 50/50. Copyright (c) 2013, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:4272 / 4280
页数:9
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