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A method of preparing a hydrogenation catalyst, for example, a phthalate hydrogenation catalyst, comprising contacting a silica support having a median pore size of at least about 10 nm with a silylating agent to form an at least partially coated silica support, calcining said coated silica support

A method of preparing a hydrogenation catalyst, for example, a phthalate hydrogenation catalyst, comprising contacting a silica support having a median pore size of at least about 10 nm with a silylating agent to form an at least partially coated silica support, calcining said coated silica support to form a treated silica support, and depositing a noble metal, preferably ruthenium, on the treated silica support, and optionally contacting the treated silica support with an optional chelating agent to form the hydrogenation catalyst; 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.

대표청구항 ▼

1. A method for the preparation of a silica-supported noble metal hydrogenation catalyst comprising the steps of: (a) providing a silica support having a median pore size of at least about 10 nm;(b) steam treating said silica support to increase the hydroxyl concentration on the surface of said sili

1. A method for the preparation of a silica-supported noble metal hydrogenation catalyst comprising the steps of: (a) providing a silica support having a median pore size of at least about 10 nm;(b) steam treating said silica support to increase the hydroxyl concentration on the surface of said silica support after streaming to produce a steamed silica support;(c) contacting said streamed silica support with a silylating agent to coat at least part of said streamed silica support to produce a coated silica support;(d) calcining said coated silica support obtained in step (c) to produce a treated and coated silica support; and(e) dispersing a noble metal by a chelating agent on said treated and coated silica support obtained in step (d) to produce said silica-supported noble metal hydrogenation catalyst having a median pore size of at least 10 nm and no more than 300 nm. 2. The method of claim 1, wherein said noble metal is selected from the group consisting of ruthenium, rhodium, palladium, platinum, and mixtures thereof. 3. The method of claim 2, wherein said noble metal is ruthenium. 4. The method of claim 1, wherein said chelating agent has from 2 to 20 carbon atoms and comprising at least one carboxylic acid or hydroxyl functional group and at least one nitrogen-containing functional group, wherein said nitrogen-containing functional group is an amine or an imine. 5. The method of claim 1, wherein said chelating agent is triethanolamine. 6. The method of claim 1, wherein the method further comprises the step (f) of calcining said silica-supported noble metal hydrogenation catalyst produced in step (e) to produce a calcined, silica-supported noble metal hydrogenation catalyst. 7. The method of claim 1, wherein said silica support used in step (a) has a median pore size of at least about 20 nm. 8. The method of claim 1, wherein said silylating agent used in step (c) is a polysiloxane. 9. The method of claim 1, wherein said silylating agent used in step (c) is a poly(alkylaryl) siloxane. 10. The method of claim 1, wherein the surface area of said silica support, as measured by the BET method, is increased, after steps (b) thru (e), by at least about 20 m2/g compared to said surface area of said silica support used in step (a). 11. The method of claim 1, wherein said hydroxyl group concentration of the treated and coated silica support obtained in step (d) is increased by at least 1 Si—OH group per nm2 as compared to that of the silica support used in step (a). 12. The method of claim 1, wherein said silica-supported noble metal hydrogenation catalyst has a hydrogen to noble metal chemisorption ratio of at least about 0.50. 13. The method of claim 1, wherein said silica support used in step (a) has a crush strength of at least 800 g/mm. 14. The method of claim 1, further comprising the step of activating said silica-supported noble metal hydrogenation catalyst produced in step (e) by contacting said catalyst with hydrogen gas. 15. The method of claim 6, further comprising the step of activating said calcined, silica-supported noble metal hydrogenation catalyst produced in step (f) by contacting said catalyst with hydrogen gas.