Method of oxidative dehydrogenation of hydrocarbon compounds

US10125061B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10125061-B2
Application numberUS-201715487155-A
CountryUS
Kind codeB2
Filing dateApr 13, 2017
Priority dateApr 13, 2017
Publication dateNov 13, 2018
Grant dateNov 13, 2018

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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Abstract

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A method of oxidative dehydrogenating a butane-containing hydrocarbon stream by contacting the same with a bimetallic catalyst in the presence of an oxidant, wherein the bimetallic catalyst comprises nickel and bismuth on a titanium carbide catalyst support. Various embodiments of the method of oxidative dehydrogenating the butane-containing hydrocarbon stream and the bimetallic catalyst are also provided.

First claim

Opening claim text (preview).

The invention claimed is: 1. A method of dehydrogenating a butane-containing hydrocarbon stream, comprising: contacting the butane-containing hydrocarbon stream with a bimetallic catalyst in the presence of oxygen to form a product stream comprising a butene compound, wherein the bimetallic catalyst consists of nickel oxide and bismuth oxide on a titanium carbide catalyst support. 2. The method of claim 1 , wherein the butene compound is one or more of 1-butene, cis-2-butene, trans-2-butene, 1,3-butadiene, and isobutylene. 3. The method of claim 1 , wherein a weight percent of nickel in the bimetallic catalyst is within a range of 15 wt % to 25 wt %, relative to the total weight of the bimetallic catalyst. 4. The method of claim 1 , wherein a weight percent of bismuth in the bimetallic catalyst is within a range of 25 wt % to 35 wt %, relative to the total weight of the bimetallic catalyst. 5. The method of claim 1 , wherein the butane-containing hydrocarbon stream is contacted with the bimetallic catalyst at a temperature of 400 to 450° C. 6. The method of claim 1 , wherein a volume fraction of butane in the butane-containing hydrocarbon stream is at least 0.9. 7. The method of claim 1 , wherein a molar ratio of oxygen to butane is in a range of 1:1 to 4:1. 8. The method of claim 1 , wherein the bimetallic catalyst has an average particle size in a range of 0.1 to 2 mm. 9. The method of claim 1 , wherein the product stream further comprises non-butene compounds, and wherein a molar ratio of the butene compound to the non-butene compounds is at least 0.8. 10. The method of claim 1 , wherein a conversion of butane is in a range of 5 to 30 mol %, and wherein a yield of the butene compound is in a range of 5% to 20% based on the conversion of butane. 11. The method of claim 1 , further comprising: treating the bimetallic catalyst with an inert gas having a temperature in a range of 300 to 500° C. prior to the contacting. 12. The method of claim 1 , further comprising: mixing the butane-containing hydrocarbon stream with an inert gas to form a gaseous mixture prior to the contacting, wherein a volume fraction of the butane-containing hydrocarbon stream in the gaseous mixture is within a range of 0.01 to 0.1. 13. The method of claim 1 , wherein the butane-containing hydrocarbon stream is contacted with the bimetallic catalyst at a temperature of 400 to 450° C., and wherein a molar ratio of oxygen to butane is in a range of 1:1 to 4:1. 14. A method of dehydrogenating a butane-containing hydrocarbon stream, comprising: contacting the butane-containing hydrocarbon stream with a bimetallic catalyst in the presence of oxygen to form a product stream comprising a butene compound, wherein the bimetallic catalyst comprises nickel and bismuth on a titanium carbide catalyst support, and wherein the butane-containing hydrocarbon stream is contacted with the bimetallic catalyst at a temperature of 400 to 450° C. 15. The method of claim 14 , wherein a molar ratio of oxygen to butane is in a range of 1:1 to 4:1.

Assignees

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Classifications

  • Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

  • Mixing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

  • Arsenic, antimony or bismuth · CPC title

  • Carbon · CPC title

  • Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst · CPC title

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What does patent US10125061B2 cover?
A method of oxidative dehydrogenating a butane-containing hydrocarbon stream by contacting the same with a bimetallic catalyst in the presence of an oxidant, wherein the bimetallic catalyst comprises nickel and bismuth on a titanium carbide catalyst support. Various embodiments of the method of oxidative dehydrogenating the butane-containing hydrocarbon stream and the bimetallic catalyst are al…
Who is the assignee on this patent?
Univ King Fahd Pet & Minerals
What technology area does this patent fall under?
Primary CPC classification C07C5/48. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Nov 13 2018 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).