INFLUENCE OF CELL COMPONENTS STRUCTURE ON COUPLING PHENOMENA IN SINGLE CELL OF POLYMER ELECTROLYTE FUEL CELL

被引:0
作者
Nishimura, Akira [1 ]
Morimoto, Atsushi [1 ]
Tanaka, Shigeki [1 ]
Oshima, Atsushi [1 ]
Hirota, Masafumi [1 ]
Tohma, Eiji [2 ]
Kimura, Yukio [2 ]
Narita, Masahiko [2 ]
机构
[1] Mie Univ, Grad Sch Engn, Div Mech Engn, 1577 Kurimamachiya Cho, Tsu, Mie 5148507, Japan
[2] TOHO GAS CO LTD, Tech Res Inst, Fuel Cell Grp, Tokai, Aichi 4768501, Japan
来源
PROCEEDINGS OF THE ASME/JSME 8TH THERMAL ENGINEERING JOINT CONFERENCE 2011, VOL 2 | 2011年
关键词
PEFC; Heat and Mass Transfer Phenomena; Cell Components Structure; Simulation; Thermograph; GAS-DIFFUSION LAYER; OPTIMAL SEPARATOR SHAPE; LIQUID WATER TRANSPORT; INHOMOGENEOUS COMPRESSION; TEMPERATURE DISTRIBUTION; MODEL PREDICTIONS; PEMFC; FLOW;
D O I
暂无
中图分类号
TH [机械、仪表工业];
学科分类号
0802 ;
摘要
The purpose of this study is to point out the dominant factor of heat and mass distribution in single cell of polymer electrolyte fuel cell (PEFC). The numerical simulation by simple 3D model of PEFC has been investigated to clarify the influence of cell components structure on heat and mass transfer phenomena in PEFC. In addition, the power generation experiment and the measurement of in-plane temperature distribution by thermograph were carried out. From the simulation results, the gas channel pitch of separator was the key factor to unify in-plane distribution of temperature and gas concentration on the reaction surface. The compression of gas diffusion layer (GDL) by cell binding caused wider distribution of mass concentration in GDL. According to the experimental results, the power generation performance was promoted with the decrease in gas channel pitch irrespective of relative humidity of supply gas. In addition, the temperature range in observation area was lower with the decrease in gas channel pitch.
引用
收藏
页码:415 / +
页数:2
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