The genesis of the active phase in Raney-type catalysts: the role of leaching parameters

• Published in: Applied catalysis. A, General General, 2003-05, Vol.244 (2), p.291-300
• Main Authors: Devred, F, Hoffer, B.W, Sloof, W.G, Kooyman, P.J, van Langeveld, A.D, Zandbergen, H.W
• Format: Article
• Language: English
• Subjects: Catalysis; Catalysts: preparations and properties; Chemistry; Exact sciences and technology; General and physical chemistry; HRTEM; Leaching process; Nickel aluminium alloy; Raney-type nickel catalysts; SEM; Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry
• ISSN: 0926-860X; 1873-3875
• DOI: 10.1016/S0926-860X(02)00601-4

The morphology and microstructure of two commercial 50–50 wt.% nickel aluminium alloys (A and B) have been studied. As expected from the phase diagram, NiAl 3, Ni 2Al 3 and a small amount of metallic aluminium were observed. The distribution of the two main phases consists of a core of Ni 2Al 3 with a shell of NiAl 3. Even if the composition of the starting alloys was the same, the amounts of the different phases are different: more Ni 2Al 3 and less metallic aluminium were present in alloy B. Treatment with an aqueous sodium hydroxide solution (leaching process) leads to Raney-type nickel catalyst. Different leaching times were used in order to follow an evolution in the morphology of the catalysts. The activation process is very fast and after 10 s of leaching, most of the aluminium has been leached out and is present as alumina. The longer the leaching time, the better the catalytic performance (both activity and selectivity) of the catalysts. This evolution of catalytic performance as function of time is much more pronounced in the case of catalysts issued from alloy A.