IP Library Granted Patent US 11,946,000
Granted Patent B2
US 11,946,000 · App. 17/595,512 · Granted Apr 2, 2024

Blend small amounts of pyoil into a liquid stream processed into a gas cracker

Inventors: Daryl Bitting (Longview, TX); Kenny Randolph Parker (Afton, TN); Michael Gary Polasek (Longview, TX); David Eugene Slivensky (Tatum, TX); Xianchun Wu (Longview, TX); Jerome Leonard Stavinoha, Jr. (Longview, TX)
Assignee: Eastman Chemical Company
C10G3/40C10G1/10C10G2300/1003C10G2300/301C10G2400/20C10G2400/22
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Quick Facts
Patent No.
US 11,946,000
App. No.
17/595,512
Granted
Apr 2, 2024
Kind
B2
Abstract

A hydrocarbon cracker stream is combined with recycle content pyrolysis oil to form a combined cracker stream and the combined cracker stream is cracked in a cracker furnace to provide an olefin-containing effluent. The r-pyoil can be fed to the cracker feed. More specifically the-pyoil is present in said feedstock in an amount of not more than 20% by weight, based on the total weight of the feedstock.

Claims (22)

1. A cracker feedstock composition comprising a recycle content pyrolysis oil composition (r-pyoil), wherein said r-pyoil is present in said feedstock in an amount of 5% to 20% by weight, based on the total weight of the feedstock, wherein at least 50 weight percent of said r-pyoil is obtained from the pyrolysis steam cracking of alkanes to alkenes.

2. The composition of claim 1 , wherein at least 60 weight percent of said r-pyoil is obtained from the pyrolysis of recycled waste plastic.

3. The composition of claim 2 , wherein at least 95 weight percent of said r-pyoil is obtained from the pyrolysis of recycled waste.

4. The composition of claim 3 , wherein said recycled waste comprises waste plastics, waste textiles, waste carpet fibers, waste modified cellulose, waste biomass, post-industrial waste streams, intermediate industrial waste streams, or combinations thereof.

5. The composition of claim 4 , wherein at least 70 weight percent of said r-pyoil is obtained from the pyrolysis of waste plastic.

6. The composition of claim 1 , wherein said cracker feedstock has not been hydrotreated.

7. The composition of claim 1 , wherein said r-pyoil is present in said cracker feedstock in an amount of from 10% to 20% by weight percent.

8. The composition of claim 7 , wherein said cracker feedstock composition comprises at least 60 weight percent and/or not more than 100 weight percent of non-recycle C5 to C22 hydrocarbons.

9. The composition of claim 8 , wherein said cracker feedstock has a final boiling point of not more than 360° C. and/or at least 200, ° C.

10. The composition of claim 9 , wherein not more than 25 weight percent of the cracker feedstock has a boiling point of 300° C. or more.

11. The composition of claim 10 , wherein at least 0.5 weight percent of said cracker feedstock has a boiling point of 300° C. or more.

12. The composition of claim 11 , wherein said cracker feedstock has a total C15+ content of not more than 25 weight percent, based on the total weight of the stream.

13. The composition of claim 12 , wherein said cracker feedstock has a total C15+ content of at least 0.5 weight percent, based on the total weight of the stream.

14. The composition of claim 13 , wherein said cracker feedstock has a total chlorine content of not more than 20 ppm.

15. The composition of claim 14 , wherein said cracker feedstock has a total chlorine content of at least 0.25 ppm.

16. The composition of claim 15 , wherein said r-pyoil comprises not more than about 30 weight percent total aromatics, based on the total weight of said r-pyoil.

17. The composition of claim 16 , wherein said r-pyoil comprises at least 1 weight percent of total aromatics, based on the total weight of said r-pyoil.

18. The composition of claim 17 , wherein said r-pyoil comprises at least 15 weight percent and/or not more than 80 weight percent of paraffins, based on the total weight of said r-pyoil.

19. The composition of claim 18 , wherein said cracker feedstock comprises not more than about 15 weight percent of oxygen-containing hydrocarbons.

20. A method for making one or more olefins, comprising:

(a) combining a recycle content pyrolysis oil composition (r-pyoil) with a non-recycle C5 to C22 hydrocarbon stream to form a cracker feed stream, wherein said r-pyoil is present in said cracker feed stream in an amount of 5% to 20% by weight; wherein at least 50 of said r-pyoil is obtained from the pyrolysis of recycled waste plastic; and wherein said cracker feed stream is suitable for use in a thermal steam cracking of alkanes to alkenes; and

(b) cracking said cracker feed stream in a cracker furnace to provide an olefin-containing effluent stream.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 20, 2025
From: EASTMAN CHEMICAL COMPANY
To: EXXONMOBIL PRODUCT SOLUTIONS COMPANY
Reel/Frame 073142/0954 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 25, 2022
From: BITTING, DARYL; PARKER, KENNY RANDOLPH; POLASEK, MICHAEL GARY; SLIVENSKY, DAVID EUGENE; WU, XIANCHUN; STAVINOHA, JEROME LEONARD, JR
To: EASTMAN CHEMICAL COMPANY
Reel/Frame 058754/0672 →
Continuity (2)
Provisional Application 62852371 · May 24, 2019
Related Publication 20220267679A1 · Aug 25, 2022
Cited By (1)
US 12,644,056