Device useful for hydrogenation reactions (III)
US-9415374-B2 · Aug 16, 2016 · US
US11465130B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11465130-B2 |
| Application number | US-201816609532-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 1, 2018 |
| Priority date | May 1, 2017 |
| Publication date | Oct 11, 2022 |
| Grant date | Oct 11, 2022 |
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The present invention relates to a metal powder catalyst and its use in the selective catalytic hydrogenation of organic starting materials comprising a carbon-carbon triple bond. The powder catalyst comprises a metal alloy carrier, wherein the metal alloy comprises (i) 55 weight-% (wt-%)-80 wt-%, based on the total weight of the metal alloy, of Co, and (ii) 20 wt-%-40 wt-%, based on the total weight of the metal alloy, of Cr, and (iii) 2 wt-%-10 wt-%, based on the total weight of the metal alloy, of Mo, and wherein the said metal alloy is coated by a metal oxide layer and impregnated with Pd, and is characterized in that the metal oxide layer comprises CeO2.
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The invention claimed is: 1. A method for selective catalytic hydrogenation with hydrogen of an organic starting material comprising a carbon-carbon triple bond, wherein the method comprises subjecting the organic starting material to selective catalytic hydrogenation in the presence of hydrogen and powderous catalytic system which comprises a metal alloy carrier, wherein the metal alloy of the carrier comprises, based on total weight of the metal alloy: (i) 55 wt. % to 70 wt. % of Co, (ii) 20 wt. % to 35 wt. % of Cr, (iii) 4 wt. % to 10 wt. % of Mo, wherein the metal alloy is coated by a metal oxide layer which comprises a mixture of CeO 2 and ZnO in a ratio of the CeO 2 to the ZnO of 2:1 to 1:2, and wherein the metal oxide layer is impregnated with Pd. 2. The method according to claim 1 , wherein the organic starting material is a compound of formula (I): wherein R 1 is linear or branched C 1 -C 35 alkyl or linear or branched C 5 -C 35 alkenyl moiety, wherein the C chain can be substituted, R 2 is linear or branched C 1 -C 4 alkyl, wherein the C chain can be substituted, and R 3 is H or —C(CO)C 1 -C 4 alkyl. 3. The method according to claim 1 , wherein the organic starting material is a compound selected from the group consisting of the following formulae: 4. The method according to claim 1 , wherein the hydrogen is in the form of H 2 gas. 5. The method according to claim 1 , wherein the metal alloy comprises at least one further metal selected from the group consisting of Cu, Fe, Ni, Mn, Si, Ti, Al and Nb. 6. The method according to claim 1 , wherein the metal alloy comprises carbon. 7. A powderous catalytic system which comprises a metal alloy carrier, wherein the metal alloy of the carrier comprises, based on total weight of the metal alloy: (i) 55 wt. % to 70 wt. % of Co, (ii) 20 wt. % to 35 wt. % of Cr, (iii) 4 wt. % to 10 wt. % of Mo, wherein the metal alloy is coated by a metal oxide layer which comprises a mixture of CeO 2 and ZnO in a ratio of the CeO 2 to ZnO of 2:1 to 1:2, and wherein the metal oxide layer is impregnated with Pd. 8. The powderous catalytic system according to claim 7 , wherein the metal alloy comprises at least one further metal selected from the group consisting of Cu, Fe, Ni, Mn, Si, Ti, Al and Nb. 9. The powderous catalytic system according to claim 7 , wherein the metal alloy comprises carbon.
of metal substrates · CPC title
Coatings comprising several layers · CPC title
of rare earths · CPC title
by hydrogenation of carbon-to-carbon double or triple bonds · CPC title
Chromium · CPC title
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