Design and numerical analysis of a planar anode-supported SOFC stack

被引:36
|
作者
Dong, Sang-Keun [1 ]
Jung, Woo-Nam [1 ]
Rashid, Kashif [1 ,2 ]
Kashimoto, Akiyoshi [3 ]
机构
[1] Korea Inst Energy Res, Adv Combust Lab, 152 Gajeong Ro, Daejeon 34129, South Korea
[2] Univ Sci & Technol, 217 Gajeong Ro, Daejeon 34113, South Korea
[3] MAGNEX CO LTD, 6-23-3 Nishikicho, Tachikawa, Tokyo, Japan
关键词
Planar solid oxide fuel cell; Stack; Numerical analysis; Electrochemical reaction; Electric circuit model; OXIDE FUEL-CELL; TEMPERATURE DISTRIBUTIONS; PERFORMANCE; SIMULATION; PREDICTION; MODEL;
D O I
10.1016/j.renene.2016.03.098
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In the present study, numerical simulations are conducted to examine the flow characteristics and attributes of electrochemical reactions in the stack through three-dimensional analysis using finite volume approach prior to the fabrication of the SOFC stack. The stack flow uniformity index is employed to investigate the flow uniformity whereas in the case of electrochemical modeling, different mathematical models are adopted to predict the characteristics of activation and ohmic overpotentials that occur during electrochemical reactions in the cell. The normalized mass flow rate is found almost same in each cell with flow uniformity index of 0.999. The calculated voltage and power curves under different average current densities are compared with experimental results for the model validation. The changes in the voltage and power of the SOFC stack, current density, temperature, over potential and reactants distributions in relation to varying amounts of reactants flow are also examined. The current density distribution in each cell is observed to vary along the anode flow direction. The temperature difference in each cell is almost same along the flow direction of reactants, and the irreversible resistance showed an opposite trend with a temperature distribution in each cell. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:637 / 650
页数:14
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