scholarly journals Collaborative Design for Uneven Physical Structures of Multi-Layers in PEMFC

2021 ◽  
Vol 12 (3) ◽  
pp. 148
Author(s):  
Qinwen Yang ◽  
Shujun Chen ◽  
Gang Xiao ◽  
Lexi Li

A collaborative design for the uneven distributions of a flow channel, gas diffusion layer porosity and catalyst layer porosity are newly proposed to improve the utilization ratio of the membrane electrode assembly of the proton exchange membrane fuel cell. The effects of the uneven design of the rib width and of the uneven porosity parameters of the cathode and anode gas diffusion layer and catalyst layer on the fuel cell performance were studied in detail. Numerical simulations were designed and implemented for validation. The results show that the fuel cell performance could be improved through the collaborative design of uneven distributions for different layers. The rib width gradually decreasing and the porosity of the cathode gas diffusion layer and the cathode catalyst layer gradually increasing along the fluid flow direction would contribute to a better design compared to the regular even design. The new uneven design can make the fuel penetrate into the catalyst layer in time to participate in the reaction, improve the utilization rate of the membrane electrode assembly, and greatly improve the performance of the fuel cell.

2014 ◽  
Vol 39 (36) ◽  
pp. 21177-21184 ◽  
Author(s):  
Sheng-Yu Fang ◽  
Lay Gaik Teoh ◽  
Rong-Hsin Huang ◽  
Kan-Lin Hsueh ◽  
Ko-Ho Yang ◽  
...  

2019 ◽  
Vol 44 (41) ◽  
pp. 23406-23415 ◽  
Author(s):  
P. Irmscher ◽  
D. Qui ◽  
H. Janßen ◽  
W. Lehnert ◽  
D. Stolten

2019 ◽  
Vol 323 ◽  
pp. 134808 ◽  
Author(s):  
Ji Eun Park ◽  
Jongkoo Lim ◽  
Myung Su Lim ◽  
Sungjun Kim ◽  
Ok-Hee Kim ◽  
...  

2005 ◽  
Vol 3 (1) ◽  
pp. 51-61 ◽  
Author(s):  
Qingyun Liu ◽  
Junxiao Wu

A multi-resolution simulation method was developed for the polymer electrolyte membrane (PEM) fuel cell simulation: a full 3D model was employed for the membrane and diffusion layer; a 1D+2D model was applied to the catalyst layer, that is, at each location of the fuel cell plate, the governing equations were integrated only in the direction perpendicular to the fuel cell plate; and a quasi-1D model with high numerical efficiency and reasonable accuracy was employed for the flow channels. The simulation accuracy was assessed in terms of the fuel cell polarization curves and membrane Ohmic overpotential. Overall, good agreements between the simulated results and the experimental data were obtained. However, at large current densities, with high relative humidity reactant inputs, the simulation under-predicted the fuel cell performance due to the single-phase assumption; the simulation slightly over-predicted the fuel cell performance for a dry cathode input, possibly due to the nonlinearity of the membrane properties in dehydration case. Further, a parameter study was performed under both fully humidified and relatively dry conditions for the parameters related to the cathode catalyst layer and the gas diffusion layer (GDL). It is found that the effects of liquid water in both the GDL and catalyst layer on the cell performance, and the accurate identification of the cathode catalyst layer parameters such as the cathodic transfer coefficient should be focused for future studies in order to further improve the model accuracy.


2016 ◽  
Vol 171 ◽  
pp. 200-212 ◽  
Author(s):  
Jaeman Park ◽  
Hwanyeong Oh ◽  
Yoo Il Lee ◽  
Kyoungdoug Min ◽  
Eunsook Lee ◽  
...  

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