Alpha-alumina-based catalyst and process for hydrogenation of an olefin in the presence thereof
The present invention relates to a catalyst comprising a) from 90% to 99.99% by weight of alumina in which said alumina is at least 90% by weight α-alumina and b) from 0.01% to 10% by weight of at least one metal of valency 0 selected from the group consisting of Pd, Ru, Pt, Rh and Ir, characterized in that the chloride content of said catalyst is less than 500 ppm, based on the total weight of the catalyst.
1. A catalyst comprising a) from 90% to 99.99% by weight of alumina in which said alumina is at least 90% by weight α-alumina, b) from 0.01% to 10% by weight of at least one metal of valency 0 selected from the group consisting of Pd, Ru, Pt, Rh and Ir, and c) carbon, wherein the carbon content of said catalyst is 10 ppm to 900 ppm, based on the total weight of the catalyst.
2. The catalyst as claimed in claim 1 , wherein the water content of said catalyst is less than 2% by weight, based on the total weight of the catalyst.
3. The catalyst as claimed in claim 1 , wherein the content by weight of sodium is less than 100 ppm, based on the total weight of the catalyst.
4. The catalyst as claimed in claim 1 , wherein the content by weight of antimony is less than 20 ppm, based on the total weight of the catalyst.
5. The catalyst as claimed in claim 1 , wherein:
the content by weight of gold is less than 100 ppm, based on the total weight of the catalyst, and/or
the content by weight of lead is less than 50 ppm, based on the total weight of the catalyst, and/or
the content by weight of zinc is less than 250 ppm, based on the total weight of the catalyst, and/or
the content by weight of iron is less than 50 ppm, based on the total weight of the catalyst, and/or
the content by weight of copper is less than 50 ppm, based on the total weight of the catalyst, and/or
the content by weight of magnesium is less than 50 ppm, based on the total weight of the catalyst, and/or
the content by weight of calcium is less than 50 ppm, based on the total weight of the catalyst, and/or
the content by weight of nickel is less than 50 ppm, based on the total weight of the catalyst, and/or
the content by weight of chromium is less than 10 ppm, based on the total weight of the catalyst, and/or
the content by weight of cobalt is less than 10 ppm, based on the total weight of the catalyst, and/or
the content by weight of manganese is less than 10 ppm, based on the total weight of the catalyst.
6. A process for the hydrogenation of an olefin comprising at least one fluorine atom, the process comprising bringing said olefin into contact with hydrogen in the gas phase in the presence of the catalyst as claimed in claim 1 , in order to form an alkane compound resulting from the hydrogenation of said olefin.
7. The process as claimed in claim 6 , wherein said olefin is selected from the group consisting of 1,1,2,3,3,3-hexafluoropropene, 1,2,3,3,3-pentafluoropropene, 1,1,3,3,3-pentafluoropropene, 1,3,3,3-tetrafluoropropene, 2,3,3,3-tetrafluoropropene, 1,2-dichloro-3,3,3-trifluoropropene, 1-chloro-3,3,3-trifluoropropene and 2-chloro-3,3,3-trifluoropropene.