Carbon dioxide reforming of methane to synthesis gas has been investigated over supported Ni catalysts in the temperature range of 5004350Β°C. Addition of CaO ( 10 mol%) promoter to the Nil y-A1203 resulted in an increase of reaction rate and an improvement of catalyst stability, which may be related
Reforming of methane with carbon dioxide to synthesis gas over supported Rh catalysts
β Scribed by V.A. Tsipouriari; A.M. Efstathiou; Z.L. Zhang; X.E. Verykios
- Publisher
- Elsevier Science
- Year
- 1994
- Tongue
- English
- Weight
- 617 KB
- Volume
- 21
- Category
- Article
- ISSN
- 0920-5861
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Silicon nitride supported nickel catalyst prepared by impregnation using nickel nitrate solution was employed for the carbon dioxide reforming of methane. The catalyst was tested at 800 C under atmospheric pressure. The influences of Ni loading and calcination temperature on the catalytic performanc
Thermodynamics equilibrium analysis of carbon dioxide reforming of methane combined with steam reforming to synthesis gas was studied by Gibbs free energy minimization method to understand the effects of process variables such as temperature, pressure and inlet CH 4 /H 2 O/CO 2 ratios on product dis