Carbon Dioxide Reforming of Methane over Nickel Catalyst Supported on Ceramic Foam
نویسندگان
چکیده
منابع مشابه
Carbon dioxide reforming of methane using a non thermal plasma Effect of power supply on plasma-catalyst interaction
Introduction A lot of research has been done in catalytic reforming of methane with carbon dioxide. However, the major drawback of the reaction is the cost of the process which requires temperatures between 800 and 1000°C. In these fields, significant advantages are currently expected from non traditional approaches to catalysis. One of these new approaches consists to perform the chemical acti...
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The activity of Ni supported on mesoporous SBA-15, MCM-41, KIT-6, and a sol-gel prepared Ni/γAl2O3, for catalysing methane dry reforming was investigated. The chemical and physical characteristics of the catalysts before and after catalytic testing were investigated using X-Ray diffraction, X-ray Photoemission Spectroscopy, Transmission Electron Microscopy, Scanning Electron Microscopy / Energy...
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A series of nickel-containing mesoporous silica samples (Ni-SiO₂) with different nickel content (3.1%-13.2%) were synthesized by the evaporation-induced self-assembly method. Their catalytic activity was tested in carbon dioxide reforming of methane. The characterization results revealed that the catalysts, e.g., 6.7%Ni-SiO₂, with highly dispersed small nickel particles, exhibited excellent cat...
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Article history: Received 29 March 2010 Revised 25 May 2010 Accepted 2 June 2010 Available online 8 July 2010
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Introduction Nitrogen oxides as one of the most dangerous environmental pollutant, have harmful effects on the health of people in the workplace. Today, the catalytic oxidation of nitrogen oxides is a highly efficient method for removing of this gases that has been dedicated part of researches. The aim of study was to investigate the removal efficiency of nitrogen dioxide (NO2) by nickel and...
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ژورنال
عنوان ژورنال: Journal of the Ceramic Society of Japan
سال: 1996
ISSN: 0914-5400,1882-1022
DOI: 10.2109/jcersj.104.444