A Hydrogenation Catalyst, Its Method of Preparation and Use
US-2016199814-A1 · Jul 14, 2016 · US
US2016193591A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016193591-A1 |
| Application number | US-201414916707-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 2, 2014 |
| Priority date | Oct 18, 2013 |
| Publication date | Jul 7, 2016 |
| Grant date | — |
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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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1 . A method for the preparation of a silica-supported noble metal hydrogenation catalyst 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 silica particles to produce a noble metal-containing silica support. 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 claim 1 , wherein the chelating agent further comprises at least one carboxylic acid or hydroxyl functional group. 6 . The method of claim 1 , wherein the chelating agent has from 2 to 20 carbon atoms. 7 . The method of claim 5 , 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 1 to 6 nitrogen-containing functional groups selected from the group consisting of amine and imine groups. 9 . The method of claim 1 , wherein the chelating agent is triethanolamine. 10 . 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. 11 . The method of claim 1 , wherein the liquid containing the noble metal and the chelating agent is nebulized using ultrasound. 12 . 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. 13 . 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 noble metal-containing silica support. 14 . The method of claim 1 , wherein the method further comprises the step (c) of calcining the noble metal-containing silica support produced in step (b). 15 . The method of claim 14 , further comprising the step (d) of contacting the noble metal containing silica support 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, prepared according to the method of claim 1 . 17 . The catalyst of claim 16 , wherein the noble metal hydrogenation catalyst has an average diameter of from about 0.7 mm to about 2.4 mm. 18 . The catalyst of claim 16 , wherein the noble metal hydrogenation catalyst comprising from about 0.2 wt % to about 1.0 wt % of noble metal. 19 . The catalyst of claim 16 , wherein the radial penetration of the noble metal into the silica particles is no more than about 40% of the average diameter of the silica particles. 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. 22 . 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 obtainable by the method of claim 1 . 23 . The method of claim 22 , 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
Operations & Transport · mapped topic
Operations & Transport · mapped topic
by hydrogenation of unsaturated carbon-to-carbon bonds · CPC title
Preparation of the impregnating solution · CPC title
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