Method of preparing butadiene
US-2016347685-A1 · Dec 1, 2016 · US
US2021197179A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021197179-A1 |
| Application number | US-201816756561-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 27, 2018 |
| Priority date | Nov 28, 2017 |
| Publication date | Jul 1, 2021 |
| Grant date | — |
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 oxidative dehydrogenation of butene and a method for producing the same. The catalyst for oxidative dehydrogenation of butene has a large amount of Mo—Bi phase acting as a reaction active phase on the surface, and therefore, can exhibit high catalytic activity, high conversion rate and high butadiene selectivity in the oxidative dehydrogenation of butene.
Opening claim text (preview).
1 . A catalyst for oxidative dehydrogenation of butene, which is represented by the following Composition Formula 1, wherein a surface composition of the catalyst measured by X-ray photoelectron spectroscopy, a molar content of bismuth (Bi) is higher than a molar content of cobalt (Co), Mo a Bi b Co c (M1) d (M4) e O f [Composition Formula 1] in Composition Formula 1, Mo is molybdenum, Bi is bismuth, Co is cobalt, O is oxygen, M1 is one or more Group 1 metal elements, M4 is one or more period 4 transition metal elements excluding cobalt (Co), a is from 9 to 25, b is from 0.5 to 2, c is from 1 to 10, d is from 0.01 to 1, e is from 0.5 to 5, and f is from 30 to 50. 2 . The catalyst for oxidative dehydrogenation of butene according to claim 1 , wherein the period 4 transition metal comprises at least one selected from the group consisting of titanium, vanadium, chromium, manganese, iron, nickel, copper, and zinc. 3 . The catalyst for oxidative dehydrogenation of butene according to claim 1 , wherein the Group 1 metal comprises at least one selected from the group consisting of sodium, potassium, rubidium, and cesium. 4 . The catalyst for oxidative dehydrogenation of butene according to claim 1 , wherein the catalyst satisfies the following Calculation Formula 1 BARS/BART>6, [Calculation Formula 1] in Calculation Formula 1 BARS is the molar content of bismuth/the molar content of cobalt on the catalyst surface, measured by XPS, and BART is the molar content of bismuth/the molar content of cobalt in the entire catalyst, measured by ICP-OES. 5 . A method for producing a catalyst for oxidative dehydrogenation of butene comprising producing a first coprecipitate by mixing an aqueous solution containing a cobalt salt and a period 4 transition metal salt excluding cobalt, and an aqueous solution of ammonium molybdate, and performing co-precipitation; producing a second coprecipitate by mixing an aqueous solution of bismuth (Bi) salt and ammonium molybdate and performing co-precipitation; and mixing the first coprecipitate and the second coprecipitate; wherein producing the first coprecipitate or producing the second coprecipitate is independently performed by further mixing an aqueous solution containing a Group 1 metal salt. 6 . The method for producing a catalyst for oxidative dehydrogenation of butene according to claim 5 , wherein producing the first and second coprecipitates are each independently performed under stirring at a temperature of 30° C. to 50° C. for 0.5 to 2 hours. 7 . The method for producing a catalyst for oxidative dehydrogenation of butene according to claim 5 , wherein the period 4 transition metal comprises at least one selected from the group consisting of titanium, vanadium, chromium, manganese, iron, nickel, copper, and zinc. 8 . The method for producing a catalyst for oxidative dehydrogenation of butene according to claim 5 , wherein the Group 1 metal comprises at least one selected from the group consisting of sodium, potassium, rubidium, and cesium. 9 . The method for producing a catalyst for oxidative dehydrogenation of butene according to claim 5 , further comprising drying, grinding and classification, after mixing the first coprecipitate and the second coprecipitate. 10 . The method for producing a catalyst for oxidative dehydrogenation of butene according to claim 9 , wherein as part of classifying, only particles having a size of 355 μm or less are collected.
X-ray diffraction · CPC title
characterised by their crystalline properties, e.g. semi-crystalline (catalysts comprising carbon B01J21/18; molecular sieves B01J29/00) · CPC title
characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title
Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties · CPC title
and cobalt · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.