Transient simulation of a tubular micro-solid oxide fuel cell

被引:13
作者
Amiri, Saeid [1 ]
Hayes, R. E. [1 ]
Sarkar, Partha [2 ]
机构
[1] Univ Alberta, Dept Chem & Mat Engn, Edmonton, AB T6G 2G6, Canada
[2] Alberta Innovates Technol Futures, Edmonton, AB T6N 1E4, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
SOFC; Tubular micro-solid oxide fuel cell; Transient modelling; Experimental validation; GAS CONCENTRATION IMPEDANCE; PART I; DYNAMIC-MODEL; PERFORMANCE; POWER; PLANAR; OPTIMIZATION; BEHAVIOR; MANAGEMENT; OPERATION;
D O I
10.1016/j.jpowsour.2018.10.062
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
A 2D-axisymmetric model is developed for a tubular micro-solid oxide fuel cell (T mu SOFC), detailing heat, mass, momentum, and charge transfer as well as electrochemical reactions. Thermal transients are simulated. No parameter fitting was done, and only kinetics parameters estimated in our previous work for isothermal, steady state conditions are used. Transient experiments were conducted for this study and the data are presented. The purely predictive simulation results are found to be consistent with experimental results. The model is used to simulate the transient behavior of a step in cell current and air flow. The sensitivity of transients to several parameters are simulated and discussed. It is found that in general, transients of the system were controlled by the thermal transients indicating that other transients were much faster. Therefore, a fast electric response results from a small thermal mass of the system. Two modes could be identified in the thermal transients: fast and slow; the former is found to be associated with the cell itself, while the latter was found to be due to the furnace wall surrounding the cell. A step in current resulted in a sharp drop in voltage and its gradual recovery, which is a result of the cell slowly heating up.
引用
收藏
页码:63 / 69
页数:7
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