Systems and methods for upgrading heavy oils
US-2017349846-A1 · Dec 7, 2017 · US
US10913694B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10913694-B2 |
| Application number | US-201916513948-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 17, 2019 |
| Priority date | Jul 30, 2018 |
| Publication date | Feb 9, 2021 |
| Grant date | Feb 9, 2021 |
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According to one or more embodiments presently disclosed, a method of catalytically converting polystyrene may include contacting polystyrene with a catalyst to form a product comprising ethylbenzene. The catalyst may include oxidized iron, oxidized cobalt, and oxidized copper. The catalyst may further include a mesoporous support material with pores having an average pore diameter of from 2 nm to 50 nm.
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The invention claimed is: 1. A method of catalytically converting polystyrene, the method comprising: contacting polystyrene with a catalyst to form a product comprising ethylbenzene, where the catalyst comprises: catalytic oxidized metal materials comprising: oxidized iron; oxidized cobalt; and oxidized copper; and a mesoporous support material comprising pores having an average pore diameter of from 2 nm to 50 nm, wherein a weight ratio of iron atoms:cobalt atoms:copper atoms in the catalyst is 1:0.4-0.6:0.5-0.7. 2. The method of claim 1 , where the polystyrene is in a liquid phase when contacted with the catalyst. 3. The method of claim 1 , where the polystyrene is contacted with the catalyst in an atmosphere comprising one or more of oxygen, an inert gas, or a reducing gas. 4. The method of claim 1 , where: the product comprising ethylbenzene comprises a liquid phase and a solid phase; and a weight ratio of liquid phase to solid phase is at least 2:1 at 25° C. 5. The method of claim 4 , where the liquid phase comprises greater than 60 mole percent ethylbenzene. 6. The method of claim 1 , where the polystyrene contacts the catalyst within one of a fluidized bed reactor, a continuous stirred tank reactor, a batch reactor, a stirred tank reactor, a slurry reactor, or a moving bed reactor. 7. The method of claim 1 , where the mesoporous support material comprises alumina material or silica material. 8. The method of claim 1 , where the mesoporous support material comprises gamma alumina. 9. The method of claim 1 , where at least 95 wt. % of the catalytic oxidized metal materials are a combination of the oxidized iron, the oxidized cobalt, and the oxidized copper. 10. The method of claim 1 , where at least 95 wt. % of the mesoporous support material comprises alumina. 11. The method of claim 1 , where at least 95 wt. % of the catalyst is a combination of the catalytic oxidized metal materials and the mesoporous support material. 12. A method of catalytically converting polystyrene, the method comprising: contacting a feed stream comprising polystyrene with a catalyst to form a product stream comprising ethylbenzene, where the catalyst comprises: catalytic oxidized metal materials comprising: oxidized iron; oxidized cobalt; and oxidized copper; and a mesoporous support material comprising pores having an average pore diameter of from 2 nm to 50 nm, wherein a weight ratio of iron atoms:cobalt atoms:copper atoms in the catalyst is 1:0.4-0.6:0.5-0.7. 13. The method of claim 12 , where the feed stream comprises at least 50 wt. % of polystyrene. 14. The method of claim 12 , where the product stream comprises a liquids fraction at 25° C. 15. The method of claim 12 , where the liquids fraction comprises at least 60 mole percent ethylbenzene. 16. The method of claim 12 , where: the mesoporous support material comprises alumina material. 17. The method of claim 12 , where at least 95 wt. % of the catalytic oxidized metal materials are a combination of the oxidized iron, the oxidized cobalt, and the oxidized copper. 18. The method of claim 12 , where at least 95 wt. % of the mesoporous support material comprises alumina. 19. The method of claim 1 , where the polystyrene is contacted with the catalyst at a temperature of less than 350° C. 20. The method of claim 12 , where the feed stream is contacted with the catalyst at a temperature of less than 350° C.
Cobalt · CPC title
Iron · CPC title
Copper · CPC title
Alumina · CPC title
Ethylbenzene · CPC title
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