Catalytic Activity of Ni-YSZ composite as Anode for Methane Oxidation in Solid Oxide Fuel Cells

被引:31
|
作者
Tian, Yanting [1 ]
Lu, Zhe [2 ]
Guo, Xiang [1 ]
Wu, Pingping [1 ]
机构
[1] Taiyuan Univ Technol, Coll Phys & Optoelect, Taiyuan 030024, Shanxi, Peoples R China
[2] Harbin Inst Technol, Dept Phys, Harbin 150001, Heilongjiang, Peoples R China
来源
基金
中国国家自然科学基金;
关键词
Solid Oxide Fuel Cells; Catalytic Activity; CH4/O-2; Ratio; Ni-YSZ Anode; Partial Oxidation; SINGLE-CHAMBER SOFC; OSCILLATORY BEHAVIOR; CARBON DEPOSITION; PERFORMANCE; COKING; CO2; STABILITY;
D O I
10.20964/2019.02.48
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
Natural gas has been exploited as an available energy source for solid oxide fuel cells in recent years. However, the problem of carbon deposition that forms on nickel-based anodes by using direct methane results in performance failure of cells. It is well known that the catalytic partial oxidation of methane is a good solution to suppress carbon formation. Herein, we present an investigation of the catalytic activity of Ni/YSZ cermet anodes as a function of the CH4/O-2 flow rate ratio (1 <= R-in <= 5). The behavior of methane catalytic activity was characterized using mass spectrometry (MS) and temperature-programmed oxidation (TPO). The catalytic activity of methane oxidation at 700 degrees C showed that Ni oxidation occurred at R-in <= 1.67. A basic equilibrium to prevent carbon deposition and Ni oxidation occurred at R-in <= 2.5, which exhibited the best activity among the Ni/YSZ electrodes. Through the electrochemical measurements and impedance spectroscopy analysis of the cell, it was proved that the cell possessed the lowest ohmic resistance and optimized output performance at R-in = 2.5. In addition, a stable cell operation at 0.9 V was guaranteed without serious degradation.
引用
收藏
页码:1093 / 1106
页数:14
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