Syngas production from reforming of methane with CO2 and O 2 over Ni/SrO-SiO2 catalysts in a fluidized bed reactor

International Journal of Hydrogen Energy

Volumn 29, Issue 12, 2004, Pages 1245-1251

  Jing, Qiangshan ^a,b   Lou, Hui ^a   Fei, Jinhua ^a   Hou, Zhaoyin ^a   Zheng, Xiaoming ^a  

^a ZHEJIANG UNIVERSITY   (China)

^b XINYANG NORMAL UNIVERSITY   (China)

Author keywords

Carbon dioxide; Catalytic reforming; Hydrogen; Nickel; Strontium; Synthesis gas

Indexed keywords

CARBON DIOXIDE; CATALYSIS; CATALYSTS; CHEMICAL REACTORS; COMPOSITION; FLUIDIZED BEDS; NICKEL; SILICA; TEMPERATURE PROGRAMMED DESORPTION; TRANSMISSION ELECTRON MICROSCOPY; X RAY DIFFRACTION ANALYSIS;

CATALYTIC REFORMING; FEED GAS COMPOSITION; FIXED BED REACTORS; REACTION EQUATIONS;

METHANE;

EID: 2542430102     PISSN: 03603199     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ijhydene.2004.01.012     Document Type: Article

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