Catalyst for hydrogenation reaction and preparation method for same
US-12172150-B2 · Dec 24, 2024 · US
US12533660B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12533660-B2 |
| Application number | US-202017623315-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 25, 2020 |
| Priority date | Jun 28, 2019 |
| Publication date | Jan 27, 2026 |
| Grant date | Jan 27, 2026 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
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.
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.
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
Related publications grouped by family.
Answers are generated from the same data shown on this page.