Base Metal Catalyst
US-2015360178-A1 · Dec 17, 2015 · US
US2018280940A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018280940-A1 |
| Application number | US-201815937033-A |
| Country | US |
| Kind code | A1 |
| Filing date | Mar 27, 2018 |
| Priority date | Mar 28, 2017 |
| Publication date | Oct 4, 2018 |
| Grant date | — |
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A metal oxide catalyst involved in a hydrogenation reaction in which a ketone is converted into an alcohol, a method of preparing the metal oxide catalyst, and a method of preparing an alcohol using the same are provided. The metal oxide catalyst has a spinel structure represented by the following Formula 1: XAl 2 O 4 , <Formula 1> wherein X represents nickel or copper.
Opening claim text (preview).
What is claimed is: 1 . A metal oxide catalyst involved in a hydrogenation reaction in which a ketone is converted into an alcohol, wherein the metal oxide catalyst has a spinel structure represented by the following Formula 1: XAl 2 O 4 , <Formula 1> wherein X represents nickel or copper. 2 . The metal oxide catalyst of claim 1 , wherein a content of the nickel in the metal oxide catalyst is in a range of 20 to 65% by weight. 3 . The metal oxide catalyst of claim 1 , wherein a content of the copper in the metal oxide catalyst is in a range of 20 to 65% by weight. 4 . The metal oxide catalyst of claim 1 , wherein the metal oxide catalyst has an average particle size of 100 to 1,000 nm. 5 . A method of preparing a metal oxide catalyst, comprising: (a) dissolving a nickel or copper precursor and an aluminum precursor in a polar solvent to prepare a precursor solution; (b) pyrolyzing the precursor solution while spraying the precursor solution into a reactor using a carrier gas so as to form a catalyst powder; and (c) transferring the catalyst powder to a storage tank, followed by calcining the catalyst powder in the storage tank to increase a surface area of the catalyst powder. 6 . The method of claim 5 , wherein the polar solvent in step (a) is distilled water. 7 . The method of claim 5 , wherein the pyrolysis in step (b) is carried out at a temperature of 600 to 850° C. 8 . The method of claim 5 , wherein the calcination in step (c) is carried out at a temperature of 350 to 450° C. 9 . A method of preparing an alcohol, comprising: allowing hydrogen to react with a ketone in the presence of the metal oxide catalyst defined in claim 1 to convert the ketone into an alcohol. 10 . The method of claim 9 , wherein the ketone is methyl isobutyl ketone. 11 . The method of claim 10 , wherein the alcohol is methyl isobutyl carbinol. 12 . The method of claim 9 , wherein the reaction is carried out at a temperature of 70 to 150° C. 13 . The method of claim 9 , wherein the reaction is carried out at a pressure of 0.0 to 3.0 barg. 14 . The method of claim 9 , wherein the reaction is carried out at a liquid hourly space velocity of 0.1 to 1.7 hr −1 . 15 . The method of claim 9 , wherein the ketone and the hydrogen are allowed to react at a molar ratio of 1:4 to 8.
making use of flames, plasmas or lasers · CPC title
Decomposition and pyrolysis · CPC title
Compounds of copper · CPC title
Copper · CPC title
Preparation of particles, e.g. dispersion of droplets in an oil bath · CPC title
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