WANG Run-ping, MAO Shu-hong, DUAN Xiu-qin, LIN Wen-bin, WANG Qi, CHI Yong-qing. Catalytic performance of nickel-based catalysts with different supports in partial oxidation of methane to synthesis gas[J]. Journal of Fuel Chemistry and Technology, 2015, 43(02): 228-234.
Citation: WANG Run-ping, MAO Shu-hong, DUAN Xiu-qin, LIN Wen-bin, WANG Qi, CHI Yong-qing. Catalytic performance of nickel-based catalysts with different supports in partial oxidation of methane to synthesis gas[J]. Journal of Fuel Chemistry and Technology, 2015, 43(02): 228-234.

Catalytic performance of nickel-based catalysts with different supports in partial oxidation of methane to synthesis gas

  • A series of Ni-based catalysts with different supports (Al2O3, ZrO2, CeO2, CeO2-Al2O3 and ZrO2-Al2O3) were prepared by the methods of impregnation. The effects of supports on the physical structures and catalytic performance of the resultant catalysts in partial oxidation of methane (POM) were investigated. The catalysts were characterized by N2 physical adsorption, X-ray diffraction, temperature programmed reduction by hydrogen, temperature programmed desorption of ammonia and temperature programmed oxidation. The results showed that the Ni/Al2O3 catalyst had a large BET specific surface area and high initial activity. However, the Ni/Al2O3 catalyst showed a serious deactivation due to the formation of large amount of carbon deposited on the surface of the catalyst. Ni/ZrO2 and Ni/CeO2 catalysts displayed low activity, which resulted from its low BET specific surface area and poor NiO dispersion. The Ni/ZrO2-Al2O3 catalyst showed high activity and the Ni/CeO2-Al2O3 catalyst exhibited the best activity and coking resistance among the catalysts. CeO2 could effectively suppress carbon formation and the transformation to inactive carbon species, due to the oxygen storage and release ability.
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