Modelling the effects of measured anode triple-phase boundary densities on the performance of micro-tubular hollow fiber SOFCs

被引:46
作者
Doraswami, U. [1 ]
Shearing, P. [2 ]
Droushiotis, N. [1 ]
Li, K. [1 ]
Brandon, N. P. [2 ]
Kelsall, G. H. [1 ]
机构
[1] Univ London Imperial Coll Sci Technol & Med, Dept Chem Engn, London SW7 2AZ, England
[2] Univ London Imperial Coll Sci Technol & Med, Dept Earth Sci & Engn, London SW7 2AZ, England
关键词
SOFC modelling; Anode; Hollow fibers; Triple phase boundaries; FIB-SEM; Microstructure; OXIDE FUEL-CELLS; 3-DIMENSIONAL RECONSTRUCTION; MICROSTRUCTURE; DISTRIBUTIONS; CATHODE;
D O I
10.1016/j.ssi.2009.10.013
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
The percolated or active triple phase boundary (TPB) length per unit volume of Ni-YSZ anode hollow fibers (HFs) containing 60 wt.% initial NiO and a spatially varying microstructure were measured using a focused ion beam (FIB)-SEM technique. The measured values of contiguous TPB density were interfaced with a 2-D distributed finite element model of a hollow fiber solid oxide fuel cell. The model was applied to simultaneously solve the ionic and electronic charge balances in the electrodes, which were modelled as overlying continuum materials with effective electronic and ionic conductivities. The model was used to predict the effects of anode microstructure on the distribution of current density, and anode activation polarization. Active TPB lengths of 2.63-8.63 mu m(-2) were measured for the anode depending on location in the fiber wall and local microstructure. The effective anode ionic conductivity was predicted to be crucial to spreading the reaction zone from the anode/electrolyte interface toward the anode current collector. For equal TPB distributions, faster electrochemical kinetics was predicted to constrain anode reaction current generation to within a few micrometers of the anode/electrolyte interface. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:494 / 500
页数:7
相关论文
共 35 条
[1]  
ALI A, 2006, J POWER SOURCES, V161, P965
[2]   Geometrical modeling of microstructure of solid oxide fuel cell composite electrodes [J].
Ali, Abbaspour ;
Wen, X. ;
Nandakumar, K. ;
Luo, B. Jingli ;
Chuang, Karl T. .
JOURNAL OF POWER SOURCES, 2008, 185 (02) :961-966
[3]   Definition and sensitivity analysis of a finite volume SOFC model for a tubular cell geometry [J].
Campanari, S ;
Iora, P .
JOURNAL OF POWER SOURCES, 2004, 132 (1-2) :113-126
[4]   Anode micro model of solid oxide fuel cell [J].
Chan, SH ;
Xia, ZT .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2001, 148 (04) :A388-A394
[5]   Modeling at solid oxide heat exchanger integrated stacks and simulation at high fuel utilization [J].
Costamagna, P ;
Honegger, K .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1998, 145 (11) :3995-4007
[6]   Micro-modelling of solid oxide fuel cell electrodes [J].
Costamagna, P ;
Costa, P ;
Antonucci, V .
ELECTROCHIMICA ACTA, 1998, 43 (3-4) :375-394
[7]   Comparison of different current collecting modes of anode supported micro-tubular SOFC through mathematical modeling [J].
Cui, Daan ;
Liu, Lin ;
Dong, Yonglai ;
Cheng, Mojie .
JOURNAL OF POWER SOURCES, 2007, 174 (01) :246-254
[8]   Modelling of a SOFC graded cathode [J].
Deseure, J ;
Dessemond, L ;
Bultel, Y ;
Siebert, E .
JOURNAL OF THE EUROPEAN CERAMIC SOCIETY, 2005, 25 (12) :2673-2676
[9]   Modeling Potential, Current and Gas Velocity Distributions in Micro-Tubular Hollow Fiber SOFC Stacks [J].
Doraswami, U. ;
Droushiotis, N. ;
Kelsall, G. H. .
SOLID OXIDE FUEL CELLS 11 (SOFC-XI), 2009, 25 (02) :1241-1251
[10]  
DORASWAMI U, ELECTROCHIMICA UNPUB