物理化学学报 >> 2004, Vol. 20 >> Issue (08S): 906-910.doi: 10.3866/PKU.WHXB200408zk03

研究论文 上一篇    下一篇

水蒸汽对Ni/Ce-Zr-Al-Ox催化剂上CO2-CH4反应积碳的影响

李春林;伏义路   

  1. 中国科学技术大学化学物理系,合肥 230026
  • 收稿日期:2003-08-11 修回日期:2003-11-18 发布日期:2004-08-15
  • 通讯作者: 伏义路 E-mail:flin@ustc.edu.cn

Effect on the Carbon Deposit in CO2 Reforming of CH4 over Ni/Ce-Zr-Al-Ox Catalyst by Adding Steam

Li Chun-Lin;Fu Yi-Lu   

  1. Department of Chemical Physics, University of Science and Technology of China, Hefei 230026
  • Received:2003-08-11 Revised:2003-11-18 Published:2004-08-15
  • Contact: Fu Yi-Lu E-mail:flin@ustc.edu.cn

摘要: 采用水热合成-负载法制备了Ni/Ce-Zr-Al-Ox催化剂,进行了CO2重整CH4的反应,并采用X射线光电子能谱(XPS)、程序升温加氢(TPH)等方法表征了在反应过程中催化剂表面的积碳物种,考察了添加少量水蒸汽对积碳的影响以及水蒸汽和表面积碳物种的作用. TPH实验测得有两类碳物种,一类是在250~350 ℃出现的少量α-碳,应主要是活性高的CH4解离碎片;另一类是在700 ℃附近出现的β-碳,应是导致催化剂失活的趋于石墨化或已经石墨化的积碳. β-碳比α-碳更容易同水蒸汽作用,添加少量水蒸汽到反应气中能够明显抑制β-碳的生成.活性测试结果表明, Ni/C-Zr-Al-Ox催化剂显示了89%的CH4转化率和良好的稳定性,添加3.2%(φ)的水蒸汽后活性提高到94%,由于对非活性积碳的抑制,可以预料其稳定性也将进一步提高.

关键词: Ni/Ce-Zr-Al-Ox催化剂, CO2重整CH4, 积碳, 水蒸汽, 程序升温加氢(TPH), XPS

Abstract: A Ni/Ce-Zr-Al-Ox catalyst was prepared by hydrothermal synthesis-impregnation method. The CO2 reforming of CH4 reaction was performed. By XPS and TPH methods the carbon species deposited on the surface of catalyst during the reaction were characterized; The effect on the carbon deposit by adding a small amount of steam in feed gas and the interaction between steam and carbon species were studied. The results obtained show that there are mainly two types of carbon species :α-carbon appearing at 250~350 ℃ should be mainly CH4 decomposed fragment which shows reactive to hydrogenation; β-carbon appearing at about 700 ℃ should be the unreactive carbon which tends to be graphite or is graphitized carbon and is responsible for catalyst deactivation. β-carbon is easier to react with steam than α-carbon, therefore adding a small amount of steam in feed gas can obviously suppress β-carbon deposit. The activity test shows that the Ni/Ce-Zr-Al-Ox catalyst has a CH4 conversion of 89% and a good stability, and the CH4 conversion increases to 94% by adding 3.2%(φ) steam. In addition, due to the suppression to unreactive carbon, it can be expected that the stability of catalyst will be further promoted.

Key words: Ni/Ce-Zr-Al-Ox catalyst, CO2 reforming of CH4, Carbon deposit, Steam, TPH, XPS