期刊文献+

PEMFC阴极催化剂位置与氧气传质 被引量:1

Effects of catalyst position on oxygen transport in cathode of PEMFC
下载PDF
导出
摘要 通过对PEMFC阴极活性层中反应气体(O2)的二维传质过程和电化学反应的数学模拟,研究了催化剂位置对O2传质的影响。结果表明:O2在电解质中的扩散阻力主要由O2较小的溶解度,特别是极低的扩散系数所致。催化剂位置与O2扩散阻力密切相关。少量部分被电解质覆盖的催化剂具有最好的O2传质能力,在扩散控制条件下,对整个阴极活性层性能的贡献可超过50%。大量完全被电解质覆盖的催化剂是改善活性层性能的关键。 A twodimensional mathematical model was presented considering both mass transport process and the electrochemical reaction within the cathode catalyst layer (CCL) in a proton exchange membrane fuel cell(PEMFC).The main objective was to evaluate the effects of catalyst position on oxygen transport within the CCL by solving the equations with finite element method.It was found that the great hindrance of polymer electrolyte to oxygen transport could be attributed to the small solubility and the extremely low diffusion coefficient of oxygen in the electrolyte.The model calculation revealed the obvious effects of catalyst position on oxygen transport.The catalysts,partially covered by the electrolyte,located at threephasepoint of gas,carbon and electrolyte,were observed to possess the best ability to oxygen transport.For the case of diffusion being a ratelimiting step,the contribution of the catalysts partially covered by the electrolyte to the performance of the CCL was predicted to be over 50%.The catalyst utilization efficiency could be optimized by the preferential location of platinum close to the threephasepoint. 
出处 《电池》 CAS CSCD 北大核心 2003年第3期155-157,共3页 Battery Bimonthly
关键词 PEMFC 阴极 催化剂 氧气传质 燃料电池 质于交换膜燃料电池 fuel cell proton exchange membrane catalyst oxygen transport
  • 相关文献

参考文献7

  • 1邵志刚,衣宝廉,韩明,刘浩.PEMFC膜电极三合一组件的制备方法[J].电池,2000,30(6):269-271. 被引量:6
  • 2Wilson M S, Gottesfeld S. High performance catalyzed membranes of ultra-low platinum loadings for polymer electrolyte fuel cells [J ]. J Electrochem Soc, 1992, 139(2) : L28 - L30.
  • 3Jackson R. Transport in porous catalysts[ M]. Amsterdam of Netherlands: Elsevier Scientific Publishing Company, 1977:16- 17.
  • 4Curtis M, Xianguo L. Composition and performance modeling of catalyst layer in a proton exchange membrane fuel cell [ J ]. J Power Sources, 1999, 77(1) : 17 -27.
  • 5Bernardi D M, Verbrugge M W. Mathematical model of a gas diffusion electrode bonded to a polymer electrolyte[J]. AIChE Journal, 1991,37(8):1 151-1 163.
  • 6Kulikovsky A A, Divisek J, Kornyshev A A. Modeling the cathode compartment of polymer electrolyte fuel cells:dead and active reaction zones[J] .J Electrochem Soc, 1999, 146( 11 ) : 3981 - 3991.
  • 7Porchet F, Javet P. Mass transfer phenomena at Nafion coated electrodes:limits of the membrane model[J]. Ehctrochimica Acta, 1995,40(16):2569-2577.

二级参考文献6

  • 1Qi Zhigang,J Electroana Chem,1998年,495卷,9页
  • 2Chun Younggab,J Power Sources,1998年,71卷,174页
  • 3Cleghorh S J C,J Hydrogen Energy,1997年,22卷,12期,1137页
  • 4Ye S,J Electrochem Soc,1996年,143卷,1期,L7页
  • 5邵志刚,薄层疏水催化层电极、膜电极三合一组件的制备方法[P].中国专利:991 1 2 82 6 .5 .
  • 6邵志刚,一种具有亲水、疏水复合催化层的气体扩散电极的制备方法 [P] 中国专利 :991 1 3330 7.

共引文献5

同被引文献10

引证文献1

二级引证文献3

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部