Mass transfer and water management in proton exchange membrane fuel cells with a composite foam-rib flow field

被引:17
作者
Gao, Wei [1 ]
Li, Qifeng [1 ]
Sun, Kai [1 ,2 ]
Chen, Rui [3 ]
Che, Zhizhao [1 ,2 ]
Wang, Tianyou [1 ,2 ]
机构
[1] Tianjin Univ, State Key Lab Engine, Tianjin 300350, Peoples R China
[2] Tianjin Univ, Natl Ind Educ Platform Energy Storage, Tianjin 300350, Peoples R China
[3] Loughborough Univ, Dept Aeronaut & Automot Engn, Loughborough LE11 3TU, England
基金
中国国家自然科学基金;
关键词
Composite foam-rib flow field; Mass transfer; Water management; Proton exchange membrane fuel cell; Fuel cell; HIGH-CURRENT DENSITY; METAL FOAM; MULTIPHASE SIMULATION; CHANNEL SIZE; PERFORMANCE; PEMFC; MODEL; DISTRIBUTOR; TRANSPORT; DESIGN;
D O I
10.1016/j.ijheatmasstransfer.2023.124595
中图分类号
O414.1 [热力学];
学科分类号
摘要
Mass transfer capability of reactants and hydrothermal management is important for the performance and durability of proton exchange membrane fuel cells. In the conventional rib flow field, the oxygen transport is affected by the accumulation of under-rib liquid water which causes excessive concentration loss and limits cell performance. To improve the cell performance, a composite foam-rib flow field structure is proposed by combining the metal foam flow field and the conventional rib flow field. The proposed design is simulated by using a three-dimensional homogeneous non-isothermal numerical model. The results show that the composite foam-rib flow field, by improving the oxygen transfer and water removal capabilities under the ribs, can improve the oxygen concentration and current density without increasing the pumping power, thus improving the cell performance under different conditions. The key parameters of the composite foam-rib flow field are optimized. With the optimal metal foam filling ratio of 0.75 and porosity of 0.85, the peak power density and the limiting current density for the composite foam-rib flow field are higher than the conventional rib flow field by 5.20% and 22.68%.
引用
收藏
页数:14
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