Process for making a catalyst
View Patent ↗Process for preparing a supported metal catalyst composition comprising impregnating support particles having a mean diameter of greater than 300 microns with a solution of least one catalytically active metal, or precursor thereof, such that the metal, or its precursor, is in a mobile state in the support particles; and drying the impregnated support particles. The mobile metal, or its precursor, in the support particles is then treated with a liquid comprising at least one reducing agent to deposit and immobilize the metal, or its precursor, in the support particles such that the metal, or its precursor, is distributed in the support particle in a layer below the surface of the support particle, the layer being between an inner and an outer region, each of the inner and outer regions having a lower concentration of the metal or precursor than the layer.
1. A process for preparing a supported metal catalyst composition comprising:
impregnating support particles having a mean diameter of greater than 300 microns with a solution of least one catalytically active metal, or precursor thereof, such that the metal, or its precursor, is in a mobile state in the support particles; and
drying the impregnated support particles and then treating the mobile metal, or its precursor, in the support particles with a liquid comprising at least one reducing agent to deposit and immobilize the metal, or its precursor, in the support particles such that the metal, or its precursor, is distributed in the support particle in a layer below the surface of said support particle, said layer being between an inner and an outer region, each of said inner and outer regions having a lower concentration of said metal or precursor than said layer.
2. A process as claimed in claim 1 , wherein the catalytically active metal comprises at least one Group VIII noble metal.
3. A process as claimed in claim 2 , wherein the Group VIII noble metal comprises palladium.
4. A process as claimed in claim 3 , wherein palladium is present in the catalyst composition in an amount of 0.5-2 wt %, and the concentration of reducing agent in the liquid is in excess of a molar equivalent of 2 wt % hydrazine concentration.
5. A process as claimed in claim 4 , wherein the concentration of reducing agent in the liquid is at least a molar equivalent of 3 wt % hydrazine.
6. A process as claimed in claim 5 , wherein the concentration of reducing agent in the liquid is a molar equivalent of 4-20 wt % hydrazine.
7. A process as claimed in claim 6 , wherein the concentration of reducing agent in the liquid is a molar equivalent of 4-8 wt % hydrazine.
8. A process as claimed in claim 2 , wherein the Group VIII metal comprises palladium; and the support is impregnated with at least one other promoter selected from the group consisting of gold, copper, cerium and mixtures thereof; and at least one promoter selected from the group consisting of salts of Group I, Group II, lanthanide and transition metals.
9. A process as claimed in claim 8 , wherein said inner and outer regions have a lower concentration of said promoter metal selected from the group consisting of gold, copper, cerium and mixtures thereof than said layer.
10. A process as claimed in claim 1 , wherein the reducing agent is selected from the group consisting of hydrazine, formaldehyde, sodium formate, sodium borohydride, and alcohols.
11. A process as claimed in claim 1 , wherein the support is impregnated with base.
12. A process as claimed in claim 1 , wherein the layer containing the catalytically active metal or precursor thereof has an outer edge which is at least 3% and no more than 75% of the particle radius from the surface of the support particle.
13. A process as claimed in claim 12 , wherein the layer has an average thickness of less than half the radius of the particle.
14. A process as claimed in claim 12 , wherein the layer containing the catalytically active metal or precursor thereof has an outer edge which is at least 5% of the particle radius from the surface of the support particle.
15. A process as claimed in claim 14 , wherein the layer containing the catalytically active metal or precursor thereof has an outer edge which is at least 10% of the particle radius from the surface of the support particle.
16. A process as claimed in claim 1 , wherein the layer containing the catalytically active metal or precursor thereof has an outer edge which is at least 3 microns and no more than 20 microns below the surface of each support particle.
17. A process as claimed in claim 16 , wherein the layer containing the catalytically active metal or precursor thereof has an outer edge which is 4 to 20 microns below the surface of each support particle.
18. A process as claimed in claim 17 , wherein the layer containing the catalytically active metal or precursor thereof has an outer edge which is 5 to 15 microns below the surface of each support particle.
19. A process as claimed in claim 1 , wherein the layer has an average thickness of less than half the radius of the particle.
20. A process as claimed in claim 1 , wherein the layer has an average thickness of greater than 0.1 microns.
21. A process as claimed in claim 20 , wherein the layer has an average thickness of greater than 0.1 microns and less than 25 microns.
22. A process for preparation of vinyl acetate comprising reacting ethylene and acetic acid with molecular oxygen containing gas in the presence of a catalyst composition prepared by a process as claimed in claim 1 .
23. A process as claimed in claim 22 , wherein a fluidized bed reactor is used for conducting the reaction.