Methods of reducing phosphorus content in liquid hydrocarbons
US-10011781-B2 · Jul 3, 2018 · US
US10906852B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10906852-B2 |
| Application number | US-201816500573-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 26, 2018 |
| Priority date | Apr 27, 2017 |
| Publication date | Feb 2, 2021 |
| Grant date | Feb 2, 2021 |
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.
Processes to selectively crack alkyne compounds from a hydrocarbon stream including olefinic and di-olefinic compounds are described. The process includes contacting the hydrocarbon stream with a supported CuO catalyst under conditions sufficient to crack the alkynes to form a product stream that included cracked compounds and further separating the cracked organic compounds from the hydrocarbon stream.
Opening claim text (preview).
The invention claimed is: 1. A process for removal of alkyne compounds from a hydrocarbon stream, the process comprising: contacting a hydrocarbon stream comprising 5 to 10 wt. % C 4 mono-olefins and di-olefins, 30 to 50 wt. % C 5 mono-olefins and di-olefins, 39 to 64 wt. % aromatics and paraffins, and up to 3 wt. % alkynes with a supported CuO catalyst under conditions sufficient to crack the alkynes to form a product stream comprising cracked compounds; and recovering the product stream comprising the cracked compounds. 2. The process of claim 1 , wherein the conditions sufficient to crack the alkynes to form the product stream comprising the cracked compounds comprise a temperature of 100 to 125° C. and a pressure of 0.5 MPa to 2.5 MPa at a liquid hourly space velocity of 5 to 15 h −1 . 3. The process of claim 2 , wherein the hydrocarbon stream comprises 0.2 to 0.3 wt. % of the alkynes. 4. The process of claim 1 , wherein the conditions sufficient to crack the alkynes to form the product stream comprising the cracked compounds comprise a temperature of a temperature of 160 to 185° C. and a pressure of 0.05 MPa to 0.5 MPa at a gas hourly space velocity of 280 to 400 h −1 . 5. The process of claim 4 , wherein the hydrocarbon stream comprises 0.2 to 0.3 wt. % of the alkynes. 6. The process of claim 1 , wherein the hydrocarbon feed comprises 6.5 to 7.8 wt. % C 4 mono-olefins and di-olefins, 34 to 42 wt. % C 5 mono-olefins and di-olefins, 39 to 43 wt. % C 5 paraffins, 10 to 14 wt. % isoprene, 0.2 to 0.9 wt. % alkynes, and 0.1 wt. % C 6+ compounds. 7. The process of claim 1 , wherein a support of the supported CuO catalyst comprises alumina, carbon, silica or zirconia or combinations thereof. 8. The process of claim 1 , where the supported CuO catalyst is a CuO/Al 2 O 3 catalyst. 9. The process of claim 1 , where the supported CuO catalyst further comprises one or more promoters and/or co-active compounds. 10. The process of claim 9 , wherein the promoters comprise silver (Ag), platinum (Pt), palladium (Pd), manganese (Mn), cobalt (Co), nickel (Ni), chromium (Cr), molybdenum (Mo), or mixtures thereof. 11. The process of claim 1 , wherein the hydrocarbon stream further comprises an optional inhibitor to inhibit polymerization of the C 4 and/or C 5 di-olefins. 12. The process of claim 1 , wherein the contacting further produces coke. 13. The process of claim 1 , wherein the contacting further produces hydrogen gas. 14. The process of claim 1 , wherein the alkynes comprise 2-butyne, 1-butyne, propyne, pentyne or isomers thereof, or combinations thereof. 15. The process of claim 1 , wherein the cracked compounds comprise alkanes. 16. The process of claim 15 , wherein the alkanes are methane, ethane, ethene, or mixtures thereof. 17. The process of claim 1 , wherein a di-olefin loss from the hydrocarbon stream is less than 1 wt. %. 18. The process of claim 17 , wherein the di-olefin loss is an isoprene loss. 19. The process of claim 1 , wherein the hydrocarbon stream comprises 0.2 to 0.3 wt. % of the alkynes.
Copper · CPC title
oxides; hydroxides; salts (C07C7/156 takes precedence) · CPC title
C2-C4 olefins · CPC title
Pressure · CPC title
Alumina · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.