Design and optimization of gradient wettability pore structure of adaptive PEM fuel cell cathode catalyst layer

被引:25
|
作者
Wan, Yue [1 ]
Qiu, Diankai [1 ]
Yi, Peiyun [1 ]
Peng, Linfa [1 ]
Lai, Xinmin [1 ,2 ]
机构
[1] Shanghai Jiao Tong Univ, State Key Lab Mech Syst & Vibrat, Shanghai 200240, Peoples R China
[2] Shanghai Jiao Tong Univ, Shanghai Key Lab Digital Manufacture Thin Walled, Shanghai 200240, Peoples R China
基金
中国国家自然科学基金; 上海市自然科学基金;
关键词
PEM fuel cell; MEA; Gradient catalyst layer; Water transfer; Nano-particles; PROTON-EXCHANGE MEMBRANE; PLANE POLYTETRAFLUOROETHYLENE DISTRIBUTION; GAS-DIFFUSION LAYER; NAFION CONTENT; PERFORMANCE; DEGRADATION; ELECTRODE; ENHANCEMENT; MANAGEMENT; PARTICLES;
D O I
10.1016/j.apenergy.2022.118723
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The design of cathode catalyst layer (CL) is essential to improve the mass transfer capacity of proton exchange membrane (PEM) fuel cell and increase power density. In this work, cathode CL is divided into three sub-layers, and each sub-layer is added nano-particles with different wettability. The gradient CL with hydrophilic SiO2 particles at inner layer and hydrophobic polytetrafluoroethylene (PTFE) particles at outer layer significantly enhances the performance of membrane exchange assembly (MEA). Its performance is 895 mW/cm(2)@0.6 V, which is 24.1 %higher than CL without any particles (721 mW/cm(2)@ 0.6 V). Under operating conditions of high current density, high cathode humidity and high air stoichiometry, the gradient CL has only a little voltage loss. Through Electrochemical Impedance Spectroscopies (EIS) impedance analysis under high current density (1.8A/ cm(2)), mass transfer resistance of gradient CL is 25.4 omega and is much smaller than the mass transfer resistance of the homogeneous CL of 35.1 omega, which reflects the significant enhancement in mass transfer capacity of gradient CL. The gradient catalyst layer is suitable for a wider range of current density, humidity, and stoichiometry, but excessive cathode gas stoichiometry causes a decrease in performance, which is caused by excessive drainage capacity. In addition, 18 different gradient CLs are designed and manufactured, and the gradient CL with catalyst coated membrane (CCM) structure has the best performance. In gradient CL, increasing the capillary pressure difference between sublayers is the key to performance improvement. It is confirmed that the property of MEA with appropriate wettability gradient design can be significantly improved.
引用
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页数:16
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