Phosphine-imino-quinoline and related ligands for use in ethylene oligomerization processes
US-2024360052-A1 · Oct 31, 2024 · US
US10994262B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10994262-B2 |
| Application number | US-201715765445-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 18, 2017 |
| Priority date | Jun 7, 2016 |
| Publication date | May 4, 2021 |
| Grant date | May 4, 2021 |
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Disclosed are a catalyst for oxidative dehydrogenation and a method of preparing the same. More particularly, a catalyst for oxidative dehydrogenation of butene having a high butene conversion rate and superior side reaction inhibition effect and thus having high reactivity and high selectivity for a product by preparing metal oxide nanoparticles and then fixing the prepared metal oxide nanoparticles to a support, and a method of preparing the same are provided.
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The invention claimed is: 1. A catalyst for oxidative dehydrogenation, comprising: a support consisting of one or more selected from the group consisting of silica, cordierite, titania, zirconia, silicon nitride, and silicon carbide; and a plurality of metal oxide particles having a composition of Formula 1 below and an average particle diameter of 0.1 to 50 nm uniformly coated or distributed on a surface of the support: AB 2 O 4 [Formula 1] wherein A is one or more selected from the group consisting of Cu, Ra, Ba, Sr, Ca, Be, Zn, and Mg, and B is one or more selected from the group consisting of trivalent cationic metals, and wherein the metal oxide particles are included in an amount of 5 to 20 parts by weight based on 100 parts by weight of the support, and wherein the catalyst exhibits selectivity for butadiene in an oxidative dehydrogenation conversion of butene and inhibits generation of CO and/or CO 2 as a byproduct. 2. The catalyst according to claim 1 , wherein B is one or more selected from the group consisting of Al, Fe(III), Cr, V, Ga, In, La, and Ce. 3. The catalyst according to claim 1 , wherein the catalyst is a supporting catalyst or a coating catalyst. 4. A method of preparing a catalyst for oxidative dehydrogenation, wherein the method is performed by supporting or coating a nano-scale metal oxide on a support consisting of one or more selected from the group consisting of silica, cordierite, titania, zirconia, silicon nitride, and silicon carbide, the method comprising: obtaining a mixed solution by mixing a precursor of divalent cationic metals (A), a precursor of trivalent cationic metals (B), an unsaturated fatty acid, a surfactant, and an organic solvent that is one or more selected from the group consisting of hexadecane, hexadecene, octadecane, octadecene, and octyl ether; and heating the mixed solution by elevating a temperature up to 100° C. to 120° C. at a temperature elevation rate of 1 to 10° C./min and maintaining the elevated temperature for 30 minutes to 1 hour to remove water and oxygen, followed by elevating the temperature up to 190° C. to 210° C. at a temperature elevation rate of 1 to 10° C./min and maintaining the elevated temperature for 1 hour to 2 hours, and subsequently heating up to 290° C. to 310° C. at a temperature elevation rate of 1 to 5° C./min, and then refluxing for 1 hour to 2 hours to prepare the nano-scale metal oxide having a composition of Formula 1 below and an average particle diameter of 0.1 to 50 nm: AB 2 O 4 [Formula 1] wherein A is one or more selected from the group consisting of Cu, Ra, Ba, Sr, Ca, Be, Zn, and Mg, and B is one or more selected from the group consisting of trivalent cationic metals; dispersing the nano-scale metal oxide in a solvent having a boiling point of 69° C. or less to form a dispersion of the nano-scale metal oxide; coating the dispersion of the nano-scale metal oxide on the support; and drying the support coated with the dispersion of the nano-scale metal oxide at a temperature of 40° C. to 60° C. 5. The method according to claim 4 , wherein the divalent cationic metal (A) precursor is selected from the group consisting of zinc acetate, zinc acetylacetonate, magnesium acetate, and magnesium acetylacetonate. 6. The method according to claim 4 , wherein the trivalent cationic metal (B) precursor is selected from the group consisting of aluminum acetate, aluminum acetylacetonate, iron acetate, iron acetylacetonate, chromium acetate, and chromium acetylacetonate. 7. The method according to claim 4 , wherein the divalent cationic metal (A) precursor and the trivalent cationic metal (B) precursor are mixed in a molar ratio (B/A) of 1.5 to 3. 8. The method according to claim 4 , wherein the unsaturated fatty acid is one or more selected from the group consisting of lauric acid, palmitic acid, oleic acid, and stearic acid. 9. The method according to claim 4 , wherein the surfactant is one or more selected from the group consisting of octylamine, trioctylamine, decylamine, dodecylamine, tetradecylamine, hexadecylamine, oleylamine, octadecylamine, tribenzylamine, and triphenylamine. 10. The method according to claim 4 , wherein a molar ratio of the unsaturated fatty acid to the surfactant is 1:1 to 10:1. 11. The method according to claim 4 , wherein the solvent having a boiling point of 69° C. or less is hexane or methylpentane.
with oxygen as an acceptor · CPC title
characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title
Iron · CPC title
Nanoparticles · CPC title
Scanning electron microscopy; Transmission electron microscopy · CPC title
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