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Catalytic activity and coke resistance in the carbon dioxide reforming of methane to synthesis gas over zeolite-supported Ni catalysts

โœ Scribed by Jong-San Chang; Sang-Eon Park; Hakze Chon


Publisher
Elsevier Science
Year
1996
Tongue
English
Weight
772 KB
Volume
145
Category
Article
ISSN
0926-860X

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Carbon dioxide reforming of methane to s
โœ Z.L. Zhang; X.E. Verykios ๐Ÿ“‚ Article ๐Ÿ“… 1994 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 451 KB

Carbon dioxide reforming of methane to synthesis gas has been investigated over supported Ni catalysts in the temperature range of 5004350ยฐC. 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