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Here we report on the preparation of Co/TiO 2 catalysts (8 and 16 wt % Co) using deposition precipitation by ammonia evaporation (DPA) and incipient wetness impregnation with subsequent static drying (IWI-S) and fluidized bed drying (IWI-F). Although the initial cobalt oxide dispersions were similar for catalysts with the same metal loading, the distribution of the nanoparticles over the support surface was found to increase in the order IWI-S < IWI-F < DPA. Initial activities during Fischer−Tropsch synthesis at 493 K, 20 bar were found to increase in the same order, whereas the C 5+ selectivities were significantly higher for catalysts prepared by DPA. After 200 h of Fischer− Tropsch synthesis at 35% X CO , all systems studied had lost about 20% of their initial activity, which could be completely attributed to a loss in active metal surface area, as shown by TEM histogram analysis. Deactivation constants determined using second-order deactivation kinetics were in the same order of magnitude as for Co/SiO 2 catalysts studied previously, but surprisingly, they were not affected by the distribution of cobalt. Catalysts tested at higher X CO were found to show significantly faster deactivation, which could also be attributed to cobalt particle growth.

Reaction of cis-Ru(κ 2 -OAc) 2 (PPh 3 ) 2 with two-electron donor ligands L results in the formation of complexes trans-[Ru(κ 1 -OAc)(κ 2 -OAc)L(PPh 3 ) 2 ] (L = CO, NO + , CNtBu). Vinylidene complexes (L = C=CHR) may be prepared from the corresponding reaction with terminal alkynes HCϵCR, and species containing hydroxyvinylidene ligands (L = C=CHCR 1 R 2 {OH}) may be prepared from related reactions with propargyl alcohols HCϵCCR 1 R 2 {OH}. Treatment of cis- [a]