Methane reforming over Ni/Ce-ZrO2 catalysts: effect of nickel content
暂无分享,去创建一个
Young-Sam Oh | Hyun-Seog Roh | Ki-Won Jun | K. Jun | Hyun-Seog Roh | Wen‐Sheng Dong | Wen-Sheng Dong | Young-Sam Oh | Sang Eon Park | S. Park
[1] V. Choudhary,et al. NiO/CaO‐Catalyzed Formation of Syngas by Coupled Exothermic Oxidative Conversion and Endothermic CO2 and Steam Reforming of Methane , 1994 .
[2] E. Ruckenstein,et al. Transient kinetic studies of partial oxidation of CH4 , 1996 .
[3] Andrew Dicks,et al. Hydrogen generation from natural gas for the fuel cell systems of tomorrow , 1996 .
[4] E. Ruckenstein,et al. Methane partial oxidation over NiO/MgO solid solution catalysts , 1999 .
[5] V. Choudhary,et al. Simultaneous steam and CO2 reforming of methane to syngas over NiO/MgO/SA-5205 in presence and absence of oxygen , 1998 .
[6] K. Jun,et al. Highly stable Ni catalyst supported on Ce–ZrO2 for oxy-steam reforming of methane , 2001 .
[7] A. J. Murrell,et al. Selective oxidation of methane to synthesis gas using transition metal catalysts , 1990, Nature.
[8] N. R. Udengaard,et al. Sulfur passivated reforming process lowers syngas H sub 2 /CO ratio , 1992 .
[9] V. Choudhary,et al. Selective Oxidation of Methane to CO and H2 over Ni/MgO at Low Temperatures , 1992 .
[10] C. Louis,et al. Characterization of nickel/silica catalysts during impregnation and further thermal activation treatment leading to metal particles , 1993 .
[11] Shikong Shen,et al. Mechanistic study of partial oxidation of methane to syngas over a Ni/Al2O3 catalyst , 1998 .
[12] Sang-Eon Park,et al. CO2 reforming of methane over zirconia-supported nickel catalysts, I. Catalytic specificity , 1999 .
[13] Jens R. Rostrup-Nielsen,et al. Promotion by Poisoning , 1991 .
[14] Yongwu Lu,et al. Mechanistic investigations on the partial oxidation of methane to synthesis gas over a nickel-on-alumina catalyst , 1998 .
[15] Daniel A. Hickman,et al. Synthesis gas formation by direct oxidation of methane over Pt monoliths , 1992 .
[16] V. Choudhary,et al. Oxidative Conversion of Methane to Syngas over Nickel Supported on Commercial Low Surface Area Porous Catalyst Carriers Precoated with Alkaline and Rare Earth Oxides , 1997 .
[17] K. L. Tan,et al. Partial oxidation of methane to syngas over Ni/MgO, Ni/CaO and Ni/CeO2 , 1998 .
[18] Malcolm L. H. Green,et al. Partial oxidation of methane to synthesis gas using carbon dioxide , 1991, Nature.
[19] Calvin H. Bartholomew,et al. The stoichiometry of hydrogen and carbon monoxide chemisorption on alumina- and silica-supported nickel , 1980 .
[20] R. Jin,et al. Mechanism for catalytic partial oxidation of methane to syngas over a Ni/Al2O3 catalyst , 2000 .
[21] J. Moulijn,et al. Temperature-programmed reduction of NiOWO3/Al2O3 Hydrodesulphurization catalysts , 1989 .
[22] R. Molina,et al. α-Alumina-Supported Nickel Catalysts Prepared from Nickel Acetylacetonate: A TPR Study , 1998 .
[23] Julian R.H. Ross,et al. Syngas production from natural gas using ZrO2-supported metals , 1998 .
[24] V. Choudhary,et al. Energy efficient methane-to-syngas conversion with low H2/CO ratio by simultaneous catalytic reactions of methane with carbon dioxide and oxygen , 1995 .
[25] L. Schmidt,et al. Production of Syngas by Direct Catalytic Oxidation of Methane , 1993, Science.
[26] R. Mark Ormerod,et al. The oxidative chemistry of methane over supported nickel catalysts , 1998 .
[27] C. Au,et al. Mechanistic Studies of CH4/O2Conversion over SiO2-Supported Nickel and Copper Catalysts , 1996 .