Three-dimensional modeling of PEMFC with contaminated anode fuel

被引:48
作者
Abdollahzadeh, M. [1 ]
Ribeirinha, P. [1 ]
Boaventura, M. [1 ]
Mendes, A. [1 ]
机构
[1] Univ Porto, Fac Engn, Dept Engn Quim, LEPABE, Rua Dr Roberto Frias, P-4200465 Porto, Portugal
关键词
Numerical modeling; Anode contamination; CO poisoning; Multiphase flow; PEMFC; METHANOL STEAM REFORMER; MATHEMATICAL-MODEL; RELATIVE-HUMIDITY; CELL; EXCHANGE; CATHODE; FLOW; CO; TEMPERATURE; PERFORMANCE;
D O I
10.1016/j.energy.2018.03.162
中图分类号
O414.1 [热力学];
学科分类号
摘要
A novel transient multi-dimensional non-isothermal multiphase model for simulating PEMFC was developed. A multiphase agglomerate catalyst model was considered for the cathode catalyst layer, while in the anode catalyst layer the effect of CO and CO2 presence was taken into consideration assuming two families of catalysts, Pt/C and Pt-Ru. The model predictions were compared to experimental data found in the literature and from an in-house PEMFC. The model was able to capture accurately the steady polarization curves of PEMFCs fed with hydrogen containing different amounts of CO and CO2. Moreover, the corresponding transient voltage was accurately simulated. The results indicated that even low CO concentration in the anode fuel, leads to a considerable degradation of the fuel cell output current density. Among the tested gas diffusion layers, the ones with the highest thickness showed worst performance of the PEMFC. Results showed, that high tortuosity and low contact angle (hydrophobicity) of the gas diffusion layer, decreases the performance of the PEMFC. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:939 / 959
页数:21
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