Experimental Study of Three Channel Designs with Model Comparison in a PEM Fuel Cell

被引:44
|
作者
Mojica, F. [1 ]
Rahman, Md A. [1 ]
Mora, J. M. [2 ]
Ocon, J. D. [2 ,3 ]
Chuang, P-Y A. [1 ]
机构
[1] Univ Calif Merced, Dept Mech Engn, 5200 North Lake Rd, Merced, CA 95343 USA
[2] Univ Philippines Diliman, Coll Engn, Energy Engn Program, Quezon City 1101, Philippines
[3] Univ Philippines Diliman, Dept Chem Engn, Coll Engn, Quezon City 1101, Philippines
关键词
Flow-Field; Parallel Channel; PEMFC; Serpentine Channel; Simulation; FLOW-FIELD DESIGNS; CATALYST LAYER; 2-PHASE FLOW; BIPOLAR PLATES; PART I; PERFORMANCE; SERPENTINE; SIMULATION; PARALLEL; OPTIMIZATION;
D O I
10.1002/fuce.202000002
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
The flow field is an integral part of a proton exchange membrane fuel cell. In this work, three flow-field designs, including straight parallel, multiple channel serpentine, and single channel serpentine, are studied systematically to investigate their effects on fuel cell performance. To evaluate the characteristics of each design, relative humidity and flow rate are parametrically adjusted to evaluate performance experimentally. A finite element-based 3D steady state, single phase COMSOL computational model is employed to analyze reactant distribution and fuel cell performance. The single channel serpentine exhibits the best performance under the greatest variety of operating conditions, but also experiences the highest inlet-outlet pressure differentials. This study shows that parallel channel design has more evenly distributed reactant concentration, but is prone to liquid water accumulation, which requires high flow rate to remain stable operation under wet conditions. In summary, the multiple channel serpentine design can provide a reasonable balance between pressure drop and flow distribution with robust fuel cell operation.
引用
收藏
页码:547 / 557
页数:11
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