质子交换膜燃料电池
阴极
材料科学
离聚物
化学工程
温度控制
电化学
热的
工作(物理)
水运
电池电压
核工程
燃料电池
汽车工程
化学
电解质
热力学
复合材料
环境科学
电极
机械工程
聚合物
工程类
水流
物理化学
环境工程
物理
共聚物
作者
Stephan Strahl,Attila Husar,Paul F. Puleston,J. Riera
出处
期刊:Fuel Cells
[Wiley]
日期:2014-03-04
卷期号:14 (3): 466-478
被引量:87
标识
DOI:10.1002/fuce.201300211
摘要
Abstract The work presented in this article combines experimental analysis and theoretical studies of temperature effects on the performance of an open‐cathode, self‐humidified PEM fuel cell system for the design of optimal control strategies. The experimental analysis shows the great potential of improving the system performance by proper thermal management. The most significant temperature dependent parameter of the system under study is the exchange current density. On the one hand it is influenced positively by a temperature increase as this lowers the activation barrier. On the other hand a higher temperature causes a reduction of the electrochemical active sites in the cathode catalyst layer due to lower water content in the ionomer and primary pores. Dynamic models for fuel cell temperature, liquid water transport and the related electrochemistry have been developed and validated against the experiment. A cascaded Extremum Seeking control algorithm with a local PI controller is proposed to regulate the temperature to a fuel cell voltage maximum. However, the slow dynamics of the temperature related catalyst‐drying effect on performance complicate the optimal thermal management with model‐free control strategies.
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