催化学报 ›› 2013, Vol. 34 ›› Issue (4): 764-768.DOI: 10.1016/S1872-2067(12)60554-3

• 研究论文 • 上一篇    下一篇

Stabilities of zeolite-supported Ni catalysts for dry reforming of methane

Anis H. FAKEEHA, Wasim U. KHAN, Ahmed S. AL-FATESH, Ahmed E. ABASAEED   

  1. Chemical Engineering Department, College of Engineering, King Saud University, P.O. Box 800, Riyadh 11421, Saudi Arabia
  • 出版日期:2013-04-23 发布日期:2013-04-24
  • 通讯作者: Ahmed E. ABASAEED

Stabilities of zeolite-supported Ni catalysts for dry reforming of methane

Anis H. FAKEEHA, Wasim U. KHAN, Ahmed S. AL-FATESH, Ahmed E. ABASAEED   

  1. Chemical Engineering Department, College of Engineering, King Saud University, P.O. Box 800, Riyadh 11421, Saudi Arabia
  • Online:2013-04-23 Published:2013-04-24

摘要:

Ni/γ-Al2O3, Ni/Y-zeolite, and Ni/H-ZSM-5 catalysts were prepared using the incipient wetness impregnation method. Their catalytic performance in dry reforming of methane was studied. The fresh and used catalysts and deposited carbon were characterized using H2 temperature-programmed reduction, temperature-programmed oxidation, N2 adsorption-desorption, X-ray diffraction, and thermogravimetric analysis. The H-ZSM-5-supported Ni catalyst proved to be more stable than the other two catalysts, as it had the lowest carbon deposition.

关键词: Carbon dioxide, Dry reforming, Methane, Nickel catalyst, H-ZSM-5 zeolite, Carbon deposition

Abstract:

Ni/γ-Al2O3, Ni/Y-zeolite, and Ni/H-ZSM-5 catalysts were prepared using the incipient wetness impregnation method. Their catalytic performance in dry reforming of methane was studied. The fresh and used catalysts and deposited carbon were characterized using H2 temperature-programmed reduction, temperature-programmed oxidation, N2 adsorption-desorption, X-ray diffraction, and thermogravimetric analysis. The H-ZSM-5-supported Ni catalyst proved to be more stable than the other two catalysts, as it had the lowest carbon deposition.

Key words: Carbon dioxide, Dry reforming, Methane, Nickel catalyst, H-ZSM-5 zeolite, Carbon deposition