high activity of Ni/Si3N4 catalyst,high selectivity and remarkable resistance to coke formation in partial oxidation of methane (POM) were reported.This work is part of a broad investigation seeking nickel catalysts supported by silicon nitride with high catalytic performance for POM.The effects of nickel loading and calcination temperature on the catalytic performance were investigated with XRD,TPR and XPS.The characterization results suggested that the nickel loading and calcination temperature affected the catalyst performance via influencing surface distribution and crystallite size of active components strongly.The order of methane conversion of Ni/Si3N4 catalysts with different nickel loadings and calcination temperatures was C-10>C-15>C-5>C-1 and S(400)>S(600)>S(800) respectively.
Preparation of monodispersed core-shell Co3O4@SiO2 catalyst and its application in N2O catalytic decomposition
Heterogeneous reduction reaction of N2O by char
Preparation of nanosized nickel powder by solution reduction
Effect of nitrification duration distribution ratio in N-SBR unit on performance of A2N2 system operation
Startup and stability of A2N2 double sludge system denitrifying phosphorus removal process
Related Author
QIU Yuan
ZHAO Yongxiang
WANG Yongzhao
HU Xiaobo
LI Haitao
WANG Changzhen
JI Peng
YU Yuexi
Related Institution
Engineering Research Center of Ministry of Education for Fine Chemicals, Shanxi University
Electric Power Science Research Institute of Guangdong Power Grid Co., Ltd.
School of Energy and Power Engineering, North China Electric Power University
State Key Laboratory of Organic-Inorganic Composites, Research Center of the Ministry of Education for High Gravity Engineering and Technology, Beijing University of Chemical Technology
National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Engineering Research Center of Beijing, Beijing University of Technology