期刊文献+

Pd/ZnO催化剂的还原及其催化甲醇水蒸气重整制氢 被引量:21

Reduction of Pd/ZnO Catalyst and Its Catalytic Activity for Steam Reforming of Methanol
在线阅读 下载PDF
导出
摘要 考察了共沉淀法制备的15.9%Pd/ZnO催化剂的还原对甲醇水蒸气重整制氢反应的影响.结果显示,当催化剂的还原温度为523~573K时,523K下反应的甲醇转化率达到了41.6%,CO2选择性为94.6%,出口CO浓度为1.26%.X射线衍射结果显示,当催化剂的还原温度为523K时PdZn合金开始形成.还原温度为523~573K范围内催化剂活性的提高归因于5~14nmPdZn合金粒子的存在.用程序升温还原及X射线衍射表征手段探究了还原过程中Pd与ZnO之间的相互作用.结果表明,Pd/ZnO可能经历了PdO/ZnO→Pd/ZnC→PdznO1-x/Zno→pdZn合金/ZnO的还原过程,而部分PdZn合金在反应过程中可重新被氧化成PdZnO1-x.对反应的活性物种进行了初步探讨. The effect of reduction temperature of the coprecipitated 15.9 % Pd/ZnO catalyst on the catalytic activity for steam reforming of methanol was investigated. The results showed that methanol conversion at 523 K reached a maximum of 41.6% with a CO2 selectivity of 94.6% and an outlet CO concentration of 1.26% over the catalyst reduced at 523-573 K. X-ray diffraction analysis revealed that a PdZn alloy began to form at a reduction temperature of 523 K. The improvement in activity at reduction temperature ranging from 523 to 573 K was attributed to the formation of the PdZn alloy with crystal size of 5-14 nm. The interaction between Pd and ZnO upon reduction was also explored by means of temperature-programmed reduction and X-ray diffraction. The results demonstrated that the reduction over Pd/ZnO might undergo a process PdO/ZnO→Pd/ZnO→ PdZnOl-x/ZnO→PdZn alloy/ZnO. The PdZn alloy was found to be partially oxidized to PdZnOl-x again during the reaction. The PdZn alloy and PdZnOl-x species might be the real active species.
出处 《催化学报》 SCIE EI CAS CSCD 北大核心 2007年第3期234-238,共5页
关键词 氧化锌 负载型催化剂 甲醇水蒸气重整 钯锌合金 活性物种 还原 palldium zinc oxide supported catalyst steam reforming of methanol PdZn alloy actiye species reduction
作者简介 王艳华,女,1973年生,博士.
  • 相关文献

参考文献15

  • 1Liu Y Y,Hayakawa T,Suzuki K,Hamakawa S,Tsunoda T,Ishii T,Kumagai M.Appl Catal A,2002,223(1-2):137
  • 2Günter M M,Ressler T,Jentoft R E,Bems B.J Catal,2001,203(1):133
  • 3Zhang X R,Shi P F.J Mol Catal A,2003,194(1-2):99
  • 4Tsai A P,Yoshimura M.Appl Catal A,2001,214(2):237
  • 5Shen J P,Song Ch Sh.Catal Today,2002,77(1-2):89
  • 6Galuszka J,Pandey R N,Ahmed S.Catal Today,1998,46(2-3):83
  • 7Iwasa N,Masuda S,Ogawa N,Takezawa N.Appl Catal A,1995,125(1):145
  • 8Chin Y H,Wang Y,Dagle R A,Li X S.Fuel Process Technol,2003,83(1-3):193
  • 9Agrell J,Germani G,Jaras S G,Boutonnet M.Appl Catal A,2003,242(2):233
  • 10Usami Y,Kagawa K,Kawazoe M,Matsumura Y,Sakurai H,Haruta M.Appl Catal A,1998,171(1):123

同被引文献255

引证文献21

二级引证文献97

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