Hydrogenation catalyst and hydrogenation process
AssigneeCatalytic Distillation Technologies
InventorJ. Yong Ryu
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Abstract
A supported hydrogenation catalyst comprising (1)Pd or a Group 8 metal comprising Pd and one other Group 8 metal, preferably a Group 8 metal selected from Pt, Ir, Ru, Co or Ni, and (2) at least two metals selected from Ag, Zn or Bi, preferably Ag and at least one of Zn or Bi. Optionally the catalyst may contain K. The catalyst is supported on a porous support such as a silica, alumina, silica-alumina or carbon. The preferred supports have an average pre diameter of 180 Å with no pores smaller than 35 Å, total pore volume larger than 0.65 cc/g and preferably less than about 100 m2/g BET surface area. The catalysts are useful for the hydrogenation of unsaturated hydrocarbons such as acetylenes and diolefins in various mixed olefin streams.
Claims8
A process for the selective hydrogenation of unsaturated compounds comprising contacting a feed containing unsaturated compounds comprising acetylenes, diolefins and olefins in at least partial liquid phase with hydrogen in the presence of a catalyst for the selective hydrogenation of unsaturated compounds comprising Pd or a Group 8 metal component comprising Pd and one other Group 8 metal, Ag in the range of 0.005 to 5% by weight, Zn in the range of 0.002 to 1% by weight and Bi in the range of 0.01 to 3% by weight to selectively hydrogenate acetylenes, diolefins, or olefins supported on shaped transition alumina having an apparent bulk density of between 0.7-0.8 g/cm3 and having mixed crystalline forms of α, κ, θ, δ, ρ, η, γ, and χ, which is highly porous having average pore diameter larger than about 180Å, no pores narrower than 35 Å, total pore volume larger than about 0.65 cc/g, and BET surface area of 20 to 70 m21/g.
Dependencies are inferred from the claim text.