A WATER AND HEAT MANAGEMENT MODEL FOR PROTON-EXCHANGE-MEMBRANE FUEL-CELLS

被引:967
作者
NGUYEN, TV [1 ]
WHITE, RE [1 ]
机构
[1] UNIV S CAROLINA,DEPT CHEM ENGN,COLUMBIA,SC 29208
关键词
D O I
10.1149/1.2220792
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
Proper water and heat management are essential for obtaining high-power-density performance at high energy efficiency for proton-exchange-membrane fuel cells. A water and heat management model was developed and used to investigate the effectiveness of various humidification designs. The model accounts for water transport across the membrane by electro-osmosis and diffusion, heat transfer from the solid phase to the gas phase and latent heat associated with water evaporation and condensation in the flow channels. Results from the model showed that at high current densities (> 1 A/cm2) ohmic loss in the membrane accounts for a large fraction of the voltage loss in the cell and back diffusion of water from the cathode side of the membrane is insufficient to keep the membrane hydrated (i.e. conductive). Consequently, to minimize this ohmic loss the anode stream must be humidified, and when air is used instead of pure oxygen the cathode stream must also be humidified.
引用
收藏
页码:2178 / 2186
页数:9
相关论文
共 25 条
[1]   MATHEMATICAL-MODEL OF A GAS-DIFFUSION ELECTRODE BONDED TO A POLYMER ELECTROLYTE [J].
BERNARDI, DM ;
VERBRUGGE, MW .
AICHE JOURNAL, 1991, 37 (08) :1151-1163
[2]  
BERNARDI DM, 1989, ELECTROCHEMICAL SOC, P510
[3]  
BERNARDI DM, 1991, ELECTROCHEMICAL SOC
[4]  
EISMAN GA, 1987, FUEL CELL TECHNOLOGY, P287
[5]  
FALES JL, 1986, ELECTROCHEMICAL SOC, P179
[6]  
Felder R.M., 1978, ELEMENTARY PRINCIPLE
[7]  
FULER T, 1989, ELECTROCHEMICAL SOC, P25
[8]  
FULLER TF, 1992, OCT EL SOC CAN M TOR
[9]  
MURPHY OJ, 1992, ELECTROCHEMICAL SOC, P158
[10]  
NGUYEN T, ELECROCHEMICAL SOC S, P39