The effect of pin-type flow field plate design on the current distribution in a H2-fed polymer electrolyte fuel cell

被引:0
作者
Zaffora, Andrea [1 ]
Barbera, Orazio [2 ]
Gallo, Edoardo [1 ]
Santamaria, Monica [1 ]
Giacoppo, Giosue [2 ]
机构
[1] Univ Palermo, Dept Engn, Viale Sci,Ed 6, I-90128 Palermo, Italy
[2] Inst Adv Energy Technol Nicola Giordano, CNR ITAE, Via Salita S Lucia Sopra Contesse 5, I-98126 Messina, Italy
关键词
Polymer electrolyte fuel cell; Hydrogen; Pin-type flow field; Current distribution; Flow field plate design; CURRENT-DENSITY; BIPOLAR PLATES; OPTIMIZATION; PERFORMANCE; SERPENTINE; PARALLEL; DYNAMICS; HYDROGEN; MODEL;
D O I
10.1016/j.jpowsour.2024.235129
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The flow field plate (FFP) design is a key factor for enhancing the electrochemical performance of Polymer Electrolyte Fuel Cells (PEFCs) through optimal reactants' distribution, low-pressure drops, and efficient water removal. The effect of geometrical features of the pin-type FFP design on the electrochemical performance of a 48 cm2 H2-fed Fuel Cell (FC) was assessed through polarization curves recording and current and temperature distribution maps along the electrode active area. The study was performed by changing excess air stoichiometry and cathode relative humidity (RH). Low-pressure drops were measured using pin-type FFPs; regardless of geometrical features, they were one order of magnitude lower than those of a single-channel serpentine FFP. Channel width and number of pins greatly influenced the current distribution along the active area and, consequently, the electrochemical performance of FCs. In particular, the best electrochemical performance was reached at air stoichiometry 4 and cathode RH = 100 % by using FFP with the highest coverage factor (65%) and the lowest channel width (1 mm). Current distribution maps demonstrated that this FFP geometry led to an almost homogeneous current distribution and efficient water removal also at high current density values. On the contrary, low coverage factor (45 %) and high channel width led to worse electrochemical performances due to an uneven reactants distribution and an inefficient water removal, causing cell flooding.
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页数:11
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