metallic bipolar plates
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2022 ◽  
Vol 73 ◽  
pp. 54-66
Author(s):  
Peng Zhang ◽  
Michael P. Pereira ◽  
Bernard F. Rolfe ◽  
Daniel E. Wilkosz ◽  
Peter Hodgson ◽  
...  

Author(s):  
Marc-Vincent Müller ◽  
Maurizio Giorgio ◽  
Philipp Hausmann ◽  
Linda Kinlechner ◽  
Angelika Heinzel ◽  
...  

Energies ◽  
2021 ◽  
Vol 14 (21) ◽  
pp. 7109
Author(s):  
Chien-Ju Hung ◽  
Wei-Jen Chen ◽  
Chao-An Lin ◽  
Huan-Ruei Shiu ◽  
Bin-Hao Chen

This paper studies the effects of compression, deformation, and the contact area in the membrane electrode assembly (MEA). The electrical impedance of fuel cell stacks due to the assembly of the metallic bipolar plates is also considered. According to decades-long fuel cell (FC) assembly experience, an increase in compression force can result in adequate contact resistance, but excessive compression may cause extra contact resistance and damage to the MEA structure. The study suggests a design for improving the performance of the FC stack by proposing different fillet radii metallic bipolar plates. It is found that the appropriate fillet radius reduces contact resistance by 13% and avoids the accumulation of compression, thereby maintaining contact resistance at adequate levels. The current design proposes a simple and effective method to minimize the dimension tolerance of single fuel cell units and support sufficient compression.


Energies ◽  
2021 ◽  
Vol 14 (17) ◽  
pp. 5484
Author(s):  
Uwe Reimer ◽  
Ekaterina Nikitsina ◽  
Holger Janßen ◽  
Martin Müller ◽  
Dieter Froning ◽  
...  

Fuel cells, designed for mobile applications, should feature compact and low-weight designs. This study describes a design process that fulfills the specific needs of target applications and the production process. The key challenge for this type of metallic bipolar plate is that the combination of two plates creates three flow fields, namely an anode side, a cathode side, and a coolant. This illustrates the fact that each cell constitutes an electrochemical converter with an integrated heat exchanger. The final arrangement is comprised of plates with parallel and separate serpentine channel configurations. The anode and cathode sides are optimized for operation under dry conditions. The final plate offers an almost perfect distribution of coolant flow over the active area. The high quality of this distribution is almost independent of the coolant mass flow, even if one of the six inlet channels is blocked. The software employed (OpenFOAM and SALOME) is freely available and can be used with templates.


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