期刊文献+

有机溶胶法制备直接甲酸燃料电池用Pd/C阳极催化剂 被引量:5

Electrocatalytic Performance of Pd/C Catalyst Prepared with Organic Sol Method for Oxidation of Formic Acid
下载PDF
导出
摘要 采用改进的有机溶胶法制备了用于直接甲酸燃料电池(DFAFC)中甲酸氧化的炭载Pd(Pd/C)催化剂。制备Pd/C催化剂时,以乙醇作溶剂,SnCl2作还原剂。控制溶剂的蒸发温度就能控制Pd/C催化剂中Pd粒子的平均粒径和相对结晶度。溶剂蒸发温度与Pd/C催化剂中Pd粒子的平均粒径和相对结晶度不成正比关系。在选择合适的溶剂蒸发温度时,能制得Pd粒子的平均粒径至6.5 nm和相对结晶度至2.85的Pd/C催化剂。比较了具有不同Pd粒子的平均粒径和相对结晶度的Pd/C催化剂对甲酸氧化的电催化性能。结果发现,Pd粒子的平均粒径小和相对结晶度低的Pd/C催化剂对甲酸氧化有好的电催化性能。 Carbon supported Pd (Pd/C) catalyst for the oxidation of formic acid in the direct formic acid fuel cell (DFAFC) was prepared with an improved organic sol method. When the Pd/C catalyst is prepared via the improved organic sol method with ethanol as the solvent and SnCl2 as the reductant, the procedure is simple and the cost is low. Especially, it was found that in this method, controlling the evaporation temperature of the solvent could control the average size and the relative crystallinity of the Pd particles in the Pd/C catalyst. The evaporation temperature of the solvent is not proportional to the average size and the relative crystallinity of the Pd particles in the Pd/C catalyst. When a suitable evaporation temperature is selected, the Pd/C catalyst with the average size as small as 6. 5 nm and the relative crystallinity as low as 2.85 of the Pd particles could be obtained. It was found that the Pd/C catalyst with smaller average size and lower relative crystallinity shows a high electrocatalytic performance for the oxidation of formic acid.
出处 《应用化学》 CAS CSCD 北大核心 2007年第5期525-529,共5页 Chinese Journal of Applied Chemistry
基金 国家自然科学基金(20373068 20433060 20573057 20573029) 江苏省自然科学基金(BK2006224) 江苏省教育厅自然科学基金(05KJB150061)资助项目
关键词 甲酸 直接甲酸燃料电池 炭载Pd催化剂 有机溶胶法 formic acid, direct formic acid fuel cell, carbon supported Pd catalyst,organic sol method
  • 相关文献

参考文献19

  • 1陆天虹.直接醇类燃料电池——一种可能最早商品化的燃料电池[J].科学中国人,2005(1):51-51. 被引量:6
  • 2MAO Zong-Qiang(毛宗强),LU Tian-Hong(陆天虹),XING Wei(邢巍),SUN Gong-Quan(孙公权).Fuel Cell(燃料电池)[M].Beijing(北京):Chemical Industry Press(化学工业出版社),2005:212
  • 3Capon A,Parsons R.Electroanal Chem Interfacial Eletronanal Chem[J],1973,44:239
  • 4袁青云,唐亚文,周益明,刘长鹏,邢巍,陆天虹.甲酸作直接甲醇燃料电池替代燃料[J].应用化学,2005,22(9):929-932. 被引量:25
  • 5Lu G Q,Crown A,Wieckowski A.J Phys Chem B[J],1999,103:9 700
  • 6Weber M,Wang J T,Wasmus S,Savinell R F.J Electrochem Soc[J],1996,143:L158
  • 7Jayashree R S,Spendelow J S,Yeom J,Rastogi C,Shannon M A,Kenis P J A.Electrochim Acta[J],2005,50:4 674
  • 8Rice C,Ha S,Masel R I,Wieckowski A.J Power Source[J],2003,115:229
  • 9Ha S,Larsen R,Masel R I.J Power Source[J],2005,144:28
  • 10Xie B P,Xiong Y,Chen R M,Chen J,Cai P X.Catal Comm[J],2005,6:699

二级参考文献15

  • 1Hogarth M P,Hards G A. Platinum Metals Rev[J] ,1996,40:150.
  • 2Tricoli V. J Electrochem Soc[J] ,1998,145:3 798.
  • 3Narayanan S R,Vamos E,Surampudi S, et al. J Electrochem Soc[J] ,1997,144:4 195.
  • 4Lamy C,Lima A,Lerhun V, et al. Power Sources[J] ,2002,105:283.
  • 5Peled E,Duvdevani T,Aharon A, et al. Electrochem Solid-State Lett[ J] ,2001,4:A38.
  • 6Llorca M J,Feliu J M,Aldaz A, et al. J Electroanal Chem[J] ,1994,376:151.
  • 7Kita H,Lei H W. J Electroanal Chem[J] ,1995,388:167.
  • 8Lu G Q,Crown A,Wieckowski A. J Phys Chem[J] ,1999,B103:9 700.
  • 9Wolter O,Willsau J,Heitbaum J. J Electrochem Soc[J] ,1985,132:1 635.
  • 10Weber M,Wang J T,Wasmus S, et al. J Electrochem Soc[J] ,1996,143:L158.

共引文献26

同被引文献62

引证文献5

二级引证文献13

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