Process for the production of a gasoline with a low sulfur content
US-9222036-B2 · Dec 29, 2015 · US
US2025058303A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2025058303-A1 |
| Application number | US-202418935644-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 3, 2024 |
| Priority date | Jun 28, 2019 |
| Publication date | Feb 20, 2025 |
| Grant date | — |
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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).
1 . A method for producing a catalyst for a hydrogenation reaction, the method comprising the steps of: (a) preparing a first solution by dissolving 0.05-10 parts by weight of copper oxide and 10-50 parts by weight of a silica carrier in a solvent, based on 40-90 parts by weight of nickel oxide; (b) adding the first solution to a precipitation container and heating the first solution to a temperature of 60-100° C. while stirring; (c) preparing a second solution by mixing a pH control agent and 3-15 parts by weight of sulfur oxide, and adding the second solution dropwise to the heated first solution to prepare a precipitate; (d) washing and filtering the precipitate and drying the precipitate at a temperature of 100-200° C. for 5-24 hours to prepare a dried product; (e) calcining the prepared dried product in an air atmosphere; and (f) reducing the dried product in a hydrogen atmosphere at a temperature of 200-500° C. to prepare a reduced product. 2 . The method of claim 1 , further comprising, after the step (f), passivating the reduced product to form a passivation layer. 3 . The method of claim 2 , wherein the reduced product is passivated with a nitrogen mixed gas including 0.1-20% oxygen. 4 . The method of claim 2 , wherein the reduced product is passivated by depositing the reduced product in an organic solvent. 5 . The method of claim 2 , wherein, when the passivation layer is removed, the reduction degree of the nickel is 90% or more. 6 . The method of claim 2 , wherein, when the passivation layer is not removed, the reduction degree of the nickel is 45% or more. 7 . The method of claim 1 , wherein a pH in the step (c) of preparing the precipitate is 7-9. 8 . A hydrogenation method for contacting a hydrocarbon resin with hydrogen in the presence of the catalyst produced by the method of claim 1 . 9 . The hydrogenation method of claim 8 , wherein the hydrocarbon resin comprises at least one selected from a hydrocarbon resin including dicyclopentadiene (DCPD), a hydrocarbon resin including C 5 fraction, and a hydrocarbon resin including C 9 fraction.
Drying, e.g. preparing a suspension, adding a soluble salt and drying · CPC title
Compounds characterised by their crystallite size · CPC title
with gases containing free hydrogen · CPC title
Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
Mixing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
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