Modeling the Influence of Carbon Spheres on the Porosity of SOFC Anode Materials

被引:11
作者
Horri, Bahman Amini [1 ]
Selomulya, Cordelia [1 ]
Wang, Huanting [1 ]
机构
[1] Monash Univ, Dept Chem Engn, Clayton, Vic 3800, Australia
基金
澳大利亚研究理事会;
关键词
OXIDE FUEL-CELL; PARTICLE-SIZE DISTRIBUTION; POROUS ALUMINA CERAMICS; COMPACTION EQUATIONS; POWDER COMPRESSION; FORMING AGENT; PORE FORMERS; MICROSTRUCTURE; PERFORMANCE; STARCH;
D O I
10.1111/j.1551-2916.2011.05037.x
中图分类号
TQ174 [陶瓷工业]; TB3 [工程材料学];
学科分类号
0805 ; 080502 ;
摘要
The influence of fabrication pressure and other ceramic processing variables, including volumetric loading fraction and the particle size ratio of pore-forming agents, on the porosity of fabricated ceramic anodes, was investigated using an integrated experimental approach with mathematical modeling to differentiate the impacts of each parameter. Despite historic observation of the properties of ceramic bodies, to date, there is a lack of available models to accurately interpret the ceramic properties as a function of the processing variables. Herein, we focus on the open porosity of the solid oxide fuel cell anode prepared from NiO/YSZ (nickel oxide/yttria stabilized zirconia) as the ceramic powder and using CMS (carbon microspheres) as a pore-forming agent. A range of pore-former volumetric blend ratios (4.4%-44.6%) and different particle size ratios between NiO/YSZ and CMS (11.27, 4.29, and 0.26) were used, whereas the influence of the applied uni-axial fabrication pressure on the open porosity of sintered anode was studied in a range of atmospheric pressure up to 40 MPa. A good agreement was observed between the proposed model and the experimental data, implying that the approach could be used to determine the significant processing parameters to fabricate ceramics with desired porosity. The model could also be used to interpret the physical basis of pore formation when using a pore-forming agent in a fabricated porous ceramic body.
引用
收藏
页码:1261 / 1268
页数:8
相关论文
共 62 条
[51]  
Singhal S C., 2003, High‐temperature Solid Oxide Fuel Cells: Fundamentals, Design and Applications
[52]   A critical evaluation of the Heckel equation [J].
Sonnergaard, JM .
INTERNATIONAL JOURNAL OF PHARMACEUTICS, 1999, 193 (01) :63-71
[53]   Tortuosity in anode-supported proton conductive solid oxide fuel cell found from current flow rates and dusty-gas model [J].
Tsai, Chih-Long ;
Schmidt, V. Hugo .
JOURNAL OF POWER SOURCES, 2011, 196 (02) :692-699
[54]   THE COMPACTION AND MECHANICAL-PROPERTIES OF AGGLOMERATED MATERIALS [J].
VANDERZWAN, J ;
SISKENS, CAM .
POWDER TECHNOLOGY, 1982, 33 (01) :43-54
[55]   The role of electrode microstructure on activation and concentration polarizations in solid oxide fuel cells [J].
Virkar, AV ;
Chen, J ;
Tanner, CW ;
Kim, JW .
SOLID STATE IONICS, 2000, 131 (1-2) :189-198
[56]   The properties of powders. Part VI. The compressibility of powders. [J].
Walker, EE .
TRANSACTIONS OF THE FARADAY SOCIETY, 1923, 19 (01) :0073-0082
[57]   Monodispersed hard carbon spherules with uniform nanopores [J].
Wang, Q ;
Li, H ;
Chen, LQ ;
Huang, XJ .
CARBON, 2001, 39 (14) :2211-2214
[58]  
Webb P.A., 2001, Volume and Density Determinations for Particle Technologists
[59]   Evaluation and modeling of performance of anode-supported solid oxide fuel cell [J].
Yakabe, H ;
Hishinuma, M ;
Uratani, M ;
Matsuzaki, Y ;
Yasuda, I .
JOURNAL OF POWER SOURCES, 2000, 86 (1-2) :423-431
[60]   PARTICLE SLIPPAGE AND REARRANGEMENT DURING COMPRESSION OF PHARMACEUTICAL POWDERS [J].
YORK, P .
JOURNAL OF PHARMACY AND PHARMACOLOGY, 1978, 30 (01) :6-10