Determination of the optimal active area for proton exchange membrane fuel cells with parallel, interdigitated or serpentine designs
Determination of the optimal active area for proton exchange membrane fuel cells with parallel, interdigitated or serpentine designs
复制标题
确定具有平行、叉指或蛇形设计的质子交换膜燃料电池的最佳活性面积
DOI:
10.1016/j.ijhydene.2008.12.049
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发表时间:
2009-05
影响因子:
7.2
通讯作者:
Lee D J
中科院分区:
文献类型:
--
作者:
Zhang X X;Yan W M;Su A;Wang X D;Lee D J
Effects of active area size on steady-state characteristics of a working PEM fuel cell, including local current densities, local oxygen transport rates, and liquid water transport were studied by applying a three-dimensional, two-phase PEM fuel cell model. The PEM fuel cells were with parallel, interdigitated, and serpentine flow channel design. At high operating voltages, the size effects on cell performance are not noticeable owing to the occurrence of oxygen supply limit. The electrochemical reaction rates are high at low operating voltages, producing large quantity of water, whose removal capability is significantly affected by flow channel design. The cells with long parallel flow field experience easy water accumulation, thereby presenting low oxygen transport rate and low current density. The cells with interdigitated and serpentine flow fields generate forced convection stream to improve reactant transport and liquid water removal, thereby leading to enhanced cell performance and different size effect from the parallel flow cells. Increase in active area significantly improves performance for serpentine cells, but only has limited effect on that of interdigitated cells. Size effects of pressure drop over the PEM cells were also discussed.
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