Circulation of Ni0.15Mg0.85O catalyst particles in the fluidized bed reactor gave much higher CH4 conversion in methane reforming with CO2 and O2 under pressurized condition than the case of the catalyst without moving in the fixed bed reactor. In addition, circulation of the catalyst particles in the fluidized bed reactor inhibited carbon deposition which is the serious problem in methane reforming.
|Number of pages||5|
|Publication status||Published - 2001|
ASJC Scopus subject areas
- Process Chemistry and Technology