Modelling of CO Poisoning and its Dynamics in HTPEM Fuel Cells

被引:52
作者
Bergmann, A. [1 ]
Gerteisen, D. [1 ]
Kurz, T. [1 ]
机构
[1] Fraunhofer Inst Solar Energy Syst, D-79110 Freiburg, Germany
关键词
Anode kinetics; CO poisoning; Fuel cell; HTPEM; Mathematical Modelling; PBI; PEM; ACID DOPED POLYBENZIMIDAZOLE; ADSORPTION;
D O I
10.1002/fuce.200900128
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
In this work, a dynamic, 2-dimensional, non-isothermal model of a PBI-based HTPEM fuel cell has been developed. The model consists of a five-layer geometry with gas channels, gas diffusion layers (GDL) and membrane. The catalyst layers are taken into account as infinitesimal thin reaction layers between GDL and membrane. The overall cell behaviour is simulated considering conservation of mass, momentum, species, charge and energy. The model is focussed on CO poisoning of the anode in steady state as well as in dynamic operation. Therefore, a temperature and time-dependent approach of adsorption/desorption of CO and H-2 on the catalyst sites and the electrochemical reactions of the adsorbed species is applied. The temperature dependency of the fuel cell performance is investigated in a temperature range between 125 and 160 degrees C at pure hydrogen operation. CO poisoning of the anode is analysed with polarisation curves for different CO concentrations as well as the dynamic response during a CO pulse. The model results are validated by experimental data of in-house measurements.
引用
收藏
页码:278 / 287
页数:10
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