Hydrogen production through steam electrolysis: Control strategies for a cathode-supported intermediate temperature solid oxide electrolysis cell

被引:79
|
作者
Udagawa, J. [1 ,2 ]
Aguiar, P. [1 ]
Brandon, N. P. [1 ]
机构
[1] Univ London Imperial Coll Sci Technol & Med, Dept Earth Sci & Engn, London SW7 2AZ, England
[2] Univ London Imperial Coll Sci Technol & Med, Ctr Environm Policy, Imperial Ctr Energy Policy & Technol, London SW7 2AZ, England
关键词
hydrogen production; steam electrolyser; SOEC; intermediate temperature; planar; dynamic model;
D O I
10.1016/j.jpowsour.2008.01.069
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
Hydrogen production via steam electrolysis may involve less electrical energy consumption than conventional low temperature water electrolysis, reflecting the favourable thermodynamics and kinetics at elevated temperatures. The present paper reports on the development of a one-dimensional dynamic model of a cathode-supported planar intermediate temperature solid oxide electrolysis cell (SOEC) stack with air flow introduced through the cells. The model, which consists of an electrochemical model, two mass balances, and four energy balances, is here employed to study the prospect of the stack temperature control through the variation of the air flow rate. The simulations found that the increase in the air flow rate provides enhanced cooling and heating during exothermic and endothermic operations, respectively. The stack behaviour has suggested that such a convective heat transfer between the cell components and air flow would allow the control of stack temperature. However, only a small dependence of the temperature on the air flow rate was observed for a stack driven at conditions near thermoneutral operation, indicating that this operating mode should be avoided from a control perspective. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:354 / 364
页数:11
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