A Hydrogenation Catalyst, Its Method of Preparation and Use
US-2016199814-A1 · Jul 14, 2016 · US
US9861960B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9861960-B2 |
| Application number | US-201414916707-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 2, 2014 |
| Priority date | Oct 18, 2013 |
| Publication date | Jan 9, 2018 |
| Grant date | Jan 9, 2018 |
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A method of preparing a hydrogenation catalyst, for example, a phthalate hydrogenation catalyst, comprising nebulizing a liquid containing a noble metal and a chelating agent comprising at least one nitrogen-containing functional group to form a nebulized liquid, and contacting the nebulized liquid with silica particles; a hydrogenation catalyst prepared by that method; and a method of hydrogenating unsaturated hydrocarbons, such as phthalates, in which an unsaturated hydrocarbon is contacted with hydrogen gas in the presence of the hydrogenation catalyst of the invention.
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The invention claimed is: 1. A method for the preparation of a silica-supported noble metal hydrogenation catalyst having a radial penetration of the noble metal into silica particles of no more than about 40% of the average diameter of the silica particles in the range from about 0.7 mm to about 2.4 mm, the method comprising the steps of: (a) nebulizing a liquid containing a noble metal and a chelating agent to form a nebulized liquid, wherein the chelating agent comprises at least one nitrogen-containing functional group selected from the group consisting of amine and imine functional groups; and (b) contacting the nebulized liquid of step (a) with the silica particles to produce the silica-supported noble metal hydrogenation catalyst. 2. The method of claim 1 , wherein the noble metal is selected from the group consisting of ruthenium, rhodium, palladium, platinum, and mixtures thereof. 3. The method of claim 1 , wherein the nebulized liquid is in the form of a solution and wherein the noble metal is in the form of a noble metal salt. 4. The method of claim 3 , wherein the noble metal salt is a nitrosyl nitrate salt. 5. The method of claim 3 , wherein, in step (b), the silica particles are sprayed with a volume of the solution of the nebulized liquid corresponding to from about 20% to about 35% of the solvent absorption capacity of the silica-supported noble metal hydrogenation catalyst. 6. The method claim 1 , wherein the chelating agent further comprises at least one carboxylic acid or hydroxyl functional group. 7. The method of claim 6 , wherein the chelating agent has from 1 to 6 carboxylic acid or hydroxyl functional groups. 8. The method of claim 1 , wherein the chelating agent has from 2 to 20 carbon atoms. 9. The method of claim 1 , wherein the chelating agent has from 1 to 6 nitrogen-containing functional groups selected from the group consisting of amine and imine groups. 10. The method of claim 1 , wherein the chelating agent is triethanolamine. 11. The method of claim 1 , wherein the silica particles used in step (b) have an average diameter of no more than about 2.4 mm. 12. The method of claim 1 , wherein the liquid containing the noble metal and the chelating agent is nebulized using ultrasound. 13. The method of claim 1 , wherein the nebulized liquid containing the noble metal and the chelating agent has an average droplet size of from about 3 μm to about 40 μm. 14. The method of claim 1 , wherein the method further comprises the step (c) of calcining the silica-supported noble metal hydrogenation catalyst produced in step (b). 15. The method of claim 14 , further comprising the step (d) of contacting the silica-supported noble metal hydrogenation catalyst produced in step (b) or step (c) with hydrogen gas to form an activated silica-supported noble metal hydrogenation catalyst. 16. A silica-supported noble metal hydrogenation catalyst comprising a noble metal dispersed on silica particles and having a radial penetration of the noble metal into the silica particles of no more than about 40% of the average diameter of the silica particles in the range from about 0.7 mm to about 2.4 mm, the silica-supported noble metal hydrogenation catalyst prepared according to the method of claim 1 . 17. The silica-supported noble metal hydrogenation catalyst of claim 16 , wherein the silica-supported noble metal hydrogenation catalyst comprising from about 0.2 wt % to about 1.0 wt % of noble metal. 18. The silica-supported noble metal hydrogenation catalyst of claim 16 , wherein the noble metal is ruthenium. 19. The silica-supported noble metal hydrogenation catalyst of claim 16 , wherein the chelating agent is triethanolamine. 20. A method of hydrogenating an unsaturated hydrocarbon, comprising the step of contacting an unsaturated hydrocarbon with hydrogen gas in the presence of the silica-supported noble metal hydrogenation catalyst of claim 16 . 21. The method of claim 20 , wherein the unsaturated hydrocarbon is a phthalate.
characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title
Ruthenium · CPC title
with hydrogen or hydrogen-containing gases · CPC title
Silica · CPC title
by hydrogenation of unsaturated carbon-to-carbon bonds · CPC title
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