IP Library Granted Patent US 10,913,694
Granted Patent B2
US 10,913,694 · App. 16/513,948 · Granted Feb 9, 2021

Methods for forming ethylbenzene from polystyrene

Inventors: Nouf Mohammed Al-Jabri (Dammam, SA); Kuo-Wei Huang (Thuwal, SA)
Assignees: Saudi Arabian Oil Company; King Abdullah University of Science and Technology
C07C4/22C07C15/073C07C2521/04C07C2523/72C07C2523/745C07C2523/75
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Quick Facts
Patent No.
US 10,913,694
App. No.
16/513,948
Granted
Feb 9, 2021
Kind
B2
Abstract

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.

Claims (37)

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.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 17, 2019
From: AL-JABRI, NOUF MOHAMMED
To: SAUDI ARABIAN OIL COMPANY
Reel/Frame 049775/0305 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 17, 2019
From: HUANG, KUO-WEI
To: KING ABDULLAH UNIVERSITY OF SCIENCE AND TECHNOLOGY
Reel/Frame 049775/0443 →
Continuity (2)
Provisional Application 62711861 · Jul 30, 2018
Related Publication 20200031738A1 · Jan 30, 2020