期刊文献+

Pt/C催化剂的高压微波法制备及氢同位素交换性能研究 被引量:3

Microwave-Irradiated Polyol Method Synthesis of Pt/C Catalysts and Its Catalytic Activities for Hydrogen-Water Liquid Exchange Reaction
下载PDF
导出
摘要 以异丙醇为分散溶剂与还原剂,采用高压微波加热法制备了Pt/C催化剂,研究了不同实验条件对Pt尺寸的影响,利用XRD、TEM对催化剂进行了表征。再将Pt/C催化剂和聚四氟乙烯混合,负载至泡沫镍上得到疏水催化剂,研究其对氢-水液相催化交换反应的催化性能。结果表明:加入保护剂乙酸钠、羟基乙酸钠、柠檬酸氢二钠后,Pt/C催化剂的活性金属团聚现象减少,Pt平均尺寸明显减小(由4.4nm分别降低到2.3、2.5、2.3nm);升温速率对Pt尺寸影响较大,随着升温速率的提高,活性金属Pt的尺寸减小;而pH的变化对Pt粒子的尺寸影响较小。加入保护剂有利于氢-水交换反应的催化剂活性,Pt尺寸为2.3~4.4nm时,催化剂活性随Pt尺寸减小而提高。 Pt/C catalysts with isopropanol as both dispersant and reducing agent were synthesized by microwave-irradiated polyol method.The microstructures of the catalysts were characterized by XRD and TEM.The effects of capping agents,pH and heating rate on Pt particle size were studied.Then Pt/C catalysts were loaded on foam nickel with polytetrafluoroethylene latex to obtain hydrophobic catalysts,and their catalytic activities for hydrogen-water liquid phase exchange reaction were investigated.The results show that compared to the non-capped Pt/C catalysts,the average size of Pt particles in sodium acetate,sodium glycollate and disodium hydrogen citrate capped Pt/C catalysts decreases from 4.4 nm to 2.3,2.5,and 2.3 nm respectively,and the agglomeration of Pt particles becomes obscure.The mean size of Pt particles in Pt/C catalysts decreases evidently with the increasing of the heating rate.However,the mean sizes of Pt particles in the Pt/C catalysts prepared with different pH of the synthesis solution are similar.The activity of the hydrophobic catalysts with capping agents is high for hydrogen-water liquid exchange reaction,and is enhanced by decreasing the average particle size,in the range of 2.3-4.4 nm.
出处 《原子能科学技术》 EI CAS CSCD 北大核心 2012年第7期780-785,共6页 Atomic Energy Science and Technology
基金 国家自然科学基金资助项目(20901071) 国家磁约束聚变能研究专项资助(2011GB11102)
关键词 PT/C催化剂 保护剂 氢-水液相催化交换 Pt/C catalyst capping agent hydrogen-water liquid exchange reaction
  • 相关文献

参考文献15

  • 1CCRISTESCU I, CRISTESCU I R, TAMM U, et al.Simultaneous tritium and deuterium transfer in a water detritiation CECE facility at TLK[J].Fusion Eng Des, 2003, 69(1-4): 109-113.
  • 2PPEREVEZENTSEV A N, BELL A C, BRENNAN P D, et al.Development of a water detritiation facility for JET[J].Fusion Eng Des, 2002, 61-62: 585-589.
  • 3SSONG K M, SOHN S H, KANG D W, et al.Installation of liquid phase catalytic exchange columns for the Wolsong tritium removal facility[J].Fusion Eng Des, 2007, 82(15-24): 2 264-2 268..
  • 4SSUGIYAMA T, TANAKA M, MUNAKATA K, et al.Development of an improved LPCE column for the TLK facility with the help of the channeling stage model[J].Fusion Eng Des, 2008, 83(10-12): 1 442-1 446.
  • 5KKIM K R, LEE M S, PAEK S, et al.Operational analysis of a liquid phase catalytic exchange column for a detritiation of heavy water[J].Separation and Purification Technology, 2007, 54(3): 410-414.
  • 6SSOHN S H, LEE K J.Deactivation of hydrophobic Pt/SDBC catalyst in the WTRF LPCE column for tritium separation[J].Journal of Nuclear Science and Technology, 2006, 43(8): 874-883.
  • 7胡胜,肖成建,朱祖良,罗顺忠,王和义,罗阳明,任兴碧.氢水液相交换反应用高分散度Pt/C/FN疏水催化剂制备及Pt粒径效应研究[J].化学学报,2007,65(22):2515-2521. 被引量:7
  • 8胡胜 朱祖良 罗顺忠 等.疏水催化剂用Pt/C催化剂的制备方法.化学通报,2006,69:100-100.
  • 9BBAI Zhengyu, YANG Lin, ZHANG Jiangshan, et al.High-efficiency carbon-supported platinum catalysts stabilized with sodium citrate for methanol oxidation[J].Journal of Power Sources, 2010, 195: 2 653-2 658.
  • 10FANG B Z, CHAUDHARI N K, KIM M S, et al.Homogeneous deposition of platinum nanoparticles on carbon black for proton exchange membrane fuel cell[J].J Am Chem Soc, 2009, 131(42): 15 330-15 338.

二级参考文献147

共引文献35

同被引文献25

  • 1孙颖,王和义,桑革,罗阳明,曹伟,刘云怒,熊义富.反应堆含氚重水提氚关键技术研究进展[J].中国工程科学,2007,9(5):1-6. 被引量:9
  • 2周公度,叶宪曾,吴念祖.化学元素综论[M].北京:科学出版社,2012:115-118,270-273.
  • 3胡胜,肖成建,朱祖良,罗顺忠,王和义,罗阳明,任兴碧.氢水液相交换反应用高分散度Pt/C/FN疏水催化剂制备及Pt粒径效应研究[J].化学学报,2007,65(22):2515-2521. 被引量:7
  • 4ROLST()N J H, GALE K I. Deuterium protium isotopic fractionation between liquid water and gaseous hydrogen [J]. The Journal of Physical Chemistry, 1982, 86(13): 2 494-2 498.
  • 5HOIA.AND D F, KOONCE J E, KVET()N () K, et al. Tritium safety in the design of ITER tritium processing system[J]. Fusion Technolo gy, 1995, 28(3): 865 870.
  • 6MUNAKATA K, NISHIKAW A M, TAKEISHI T, et al. Recovery of tritium in room air by pre- cious metal catalyst with hydrophilic substrate [J]. J NuelSciTechnol, 1988, 25(4): 383-394.
  • 7PAUTROT G P. The tritium extraction faeility at the Insititute Laue-Langevin experience of op- eration with tritium[J]. Fusion Technology, 1988, 14(2): 480-483.
  • 8IONITA G, STEFANESCU I. The separation of deuterium and tritium on Pt/SDB/PS and Pt/C/ PTFE hydrophobic catalysts [J]. Fusion Tech nology, 1995, 28(9): 641-646.
  • 9ASAKURA Y, KIKUCHI M, YUSA H. New method for the hydrogen isotope exchange reac- tion in a hydrophobic catalyst bed[J]. Nuclear Science and Engineering, 1982, 80(1): 184 189.
  • 10SHIMIZU M, KIYOTA S, NINIMIYA R. Hy drogen isotope enrichment by hydrophilic Pt cat- alyst in Japan and western countries[C]//Pro- ceedings of the International Symposium on Iso- tope Separation and Chemical Exchange Uranium Enrichment. Tokyo, Japan: Is. n.], 1990: 56- 73.

引证文献3

二级引证文献8

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