Catalyst for hydrogenation reaction and method for producing same

US12533660B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-12533660-B2
Application numberUS-202017623315-A
CountryUS
Kind codeB2
Filing dateJun 25, 2020
Priority dateJun 28, 2019
Publication dateJan 27, 2026
Grant dateJan 27, 2026

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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Abstract

Official abstract text for this publication.

The present invention relates to a catalyst for a hydrogenation reaction and a method for producing the same, and more specifically, to a catalyst for a hydrogenation reaction, wherein the catalyst includes nickel oxide as an active ingredient and copper oxide and sulfur oxide as a promoter, and especially, can control a reduction degree value according to whether or not a passivation layer of a nickel metal is removed.

First claim

Opening claim text (preview).

The invention claimed is: 1. A catalyst for a hydrogenation reaction, comprising: 0.05-10 parts by weight of at least one first promoter selected from copper and copper oxide, 3-15 parts by weight of at least one second promoter selected from sulfur and sulfur oxide, and 10-50 parts by weight of a silica carrier as a support, based on 40-90 parts by weight of at least one active ingredient selected from nickel and nickel oxide, wherein a reduction degree of the at least one active ingredient is controllable according to a removal of a passivation layer, wherein the reduction degree of the at least one active ingredient is 90% or more when the passivation layer is removed, and is 45% or more when the passivation layer is not removed. 2. The catalyst for a hydrogenation reaction of claim 1 , wherein the reduction degree of the at least one active ingredient is measured by hydrogen-temperature program reduction (H 2 -TPR). 3. The catalyst for a hydrogenation reaction of claim 1 , wherein the at least one active ingredient has an average crystallite size of 3-10 nm. 4. The catalyst of claim 1 , wherein the catalyst has an average particle size (d 50 ) of 3-10 μm, and a proportion of catalyst particles having a particle size of 1 μm or less in a particle size distribution is 0.1-10% by volume. 5. The catalyst for a hydrogenation reaction of claim 1 , wherein the catalyst has a specific surface area of 150-300 m 2 /g. 6. The catalyst for a hydrogenation reaction of claim 1 , wherein the silica carrier has a specific surface area of 200-400 m 2 /g and a pore size of 3-10 nm. 7. The catalyst for a hydrogenation reaction of claim 1 , wherein the nickel forms a precipitate with the copper and the sulfur, is supported on the silica carrier, and is deposited and precipitated. 8. The catalyst for a hydrogenation reaction of claim 1 , wherein a reactant in the hydrogenation reaction is a hydrocarbon resin. 9. The catalyst for a hydrogenation reaction of claim 8 , wherein the hydrocarbon resin is at least one selected from a group consisting of a hydrocarbon resin including dicyclopentadiene (DCPD), a hydrocarbon resin including C5 fraction, and a hydrocarbon resin including C9 fraction. 10. The catalyst for a hydrogenation reaction of claim 8 , wherein the hydrocarbon resin has an APHA value of 30 or less after the hydrogenation reaction. 11. The catalyst for a hydrogenation reaction of claim 8 , wherein the hydrocarbon resin has an aromatic/olefin hydrogenation ratio of 0.1-1.0 after the hydrogenation reaction. 12. A catalyst for a hydrogenation reaction, comprising: 0.05-10 parts by weight of at least one first promoter selected from copper and copper oxide, 3-15 parts by weight of at least one second promoter selected from sulfur and sulfur oxide, and 10-50 parts by weight of a silica carrier as a support, based on 40-90 parts by weight of at least one active ingredient selected from nickel and nickel oxide, wherein a reduction degree of the at least one active ingredient is controllable according to a removal of a passivation layer, wherein the catalyst has an average particle size (d 50 ) of 3-10 μm, and a proportion of catalyst particles having a particle size of 1 μm or less in a particle size distribution is 0.1-10% by volume.

Assignees

Inventors

Classifications

  • Chemical modification of a polymer · CPC title

  • Reduction, e.g. hydrogenation · CPC title

  • with gases containing free hydrogen · CPC title

  • Decomposition of a metal salt · CPC title

  • Washing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

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What does patent US12533660B2 cover?
The present invention relates to a catalyst for a hydrogenation reaction and a method for producing the same, and more specifically, to a catalyst for a hydrogenation reaction, wherein the catalyst includes nickel oxide as an active ingredient and copper oxide and sulfur oxide as a promoter, and especially, can control a reduction degree value according to whether or not a passivation layer of …
Who is the assignee on this patent?
Hanwha Solutions Corp
What technology area does this patent fall under?
Primary CPC classification B01J23/755. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Jan 27 2026 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 2 related publications on this page (citations in our corpus or others sharing the same primary CPC).