By Narottam P. Bansal, Jonathan Salem, Dongming Zhu
Papers from the yank Ceramic Society's thirty first overseas convention on complex Ceramics and Composites, held in Daytona seashore, Florida, January 21-26, 2007. content material contains papers on fresh technical growth through nationwide laboratories, universities and personal industries on stable oxide gasoline mobilephone know-how together with SOFC part fabrics, processing, cell/stack fabrication and layout, electrochemical functionality and balance, long term chemical interactions, interface engineering, modeling, try out strategies and function analysis.Content:
Read Online or Download Advances in Solid Oxide Fuel Cells III: Ceramic and Engineering Science Proceeding, Volume 28, Issue 4 PDF
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Extra resources for Advances in Solid Oxide Fuel Cells III: Ceramic and Engineering Science Proceeding, Volume 28, Issue 4
NiO-GDC anode was a porous layer with a thickness of lOpm and there was also no delamination at ScSZINiO-GDC interfaces as well. The channel size was about 700 p m and the cell density u a s about 1000 cpsi. 7V) at 600°C usiiig the performance data of an LSM supported single cell, prepared using the same technique. Figure 5 shows the SEM photographs of LSM honeycomb edge and corner Advances in Solid Oxide Fuel Cells Ill . 45 Development of Fabrication Technology for Honeycomb-Type SOFC coated with a dense GDC layer.
H. Steel, SolidStcite lonics. 129 (2000) 95-110 " T. Otake, H. Yagami. K. Yashiro, Y. Nigara, T. Kawada, J. Mizusaki. Solid Stafe lonics, 161 (2003) 181-186 12 T. Hibino, A. Hashimoto. K. Asano, M. Yano, M. Suzuki and M. Sano. Ekcrrochem. SolidSure Lett, 5 (1 1) A242-A244 (2002). 13 T. Suzuki, T. Fujishiro and M. I. Power Sources. 163 (2007) 737742 I4 Y. Funahashi, T. Shimamori, T. Suzuki,Y. jishiro and M. Awano, J. P o n w S o t ~ c e . ~ , 163 (7007) 73 1-736 15 Y. Funahashi, T. Shimamori, T.
37 Electrochemical Evaluationof Micro-Tubular SOFC and Module for Ceramic Reactor Figure 7 shows I-V and I-P characteristics of the six-cell cube at 5OO0C, 550°C and 600'C when the anode gas was humidified 15OccmH2. In this condition, the output power was lower than the case of humidified 3OOccmH2, but the fuel utilization was higher. The output power was the highest at 550°C. At 6OO0C, the OCV and the output power are very lower than that at lower temperatures. The temperature at the vent of the cathode gas was 625°C.