Chain transfer agent removal between polyolefin polymerization reactors

Patent metadata

Field	Value
Publication number	US-9556288-B2
Application number	US-201514597475-A
Country	US
Kind code	B2
Filing date	Jan 15, 2015
Priority date	Dec 18, 2012
Publication date	Jan 31, 2017
Grant date	Jan 31, 2017

Abstract

A system and method for polymerizing olefin in the presence of a chain transfer agent in a first reactor to form a first polyolefin, discharging from the first reactor a transfer slurry having the first polyolefin and the chain transfer agent, and processing the transfer slurry in a separator to remove chain transfer agent and to provide a fluff slurry having the first polyolefin and a lower content of chain transfer agent than in the transfer slurry. The system and method provide for feeding the fluff slurry to a second reactor, polymerizing olefin in the second reactor to form a second polyolefin, and discharging from the second reactor a slurry having the second polyolefin.

First claim

What is claimed:

1. A polyolefin reactor system comprising:
a first polymerization reactor configured to polymerize olefin monomer in the presence of a chain transfer agent, and to discharge continuously a transfer slurry comprising a first polyolefin and the chain transfer agent;
a separation system configured to receive the transfer slurry and to discharge a recycle stream comprising the chain transfer agent, and to discharge continuously a fluff slurry comprising the first polyolefin;
a second polymerization reactor configured to receive the fluff slurry from the separation system and to discharge a product slurry comprising a second polyolefin, wherein the separation system is a hydrocyclone, a wash column, or a decanter.

2. The polyolefin reactor system of claim 1 , wherein the first polymerization reactor, the second polymerization reactor or a combination thereof comprise loop reactors.

3. The polyolefin reactor system of claim 2 , wherein a first loop polymerization reactor pressure provides motive force to drive the transfer slurry from the first polymerization reactor and through the separation system.

4. The polyolefin reactor system of claim 1 , wherein the chain transfer agent is hydrogen.

5. The polyolefin reactor system of claim 1 , wherein the fluff slurry discharging from the separation system comprises a lower amount of chain transfer agent than the transfer slurry, or substantially no chain transfer agent.

6. The polyolefin reactor system of claim 1 , wherein the first polyolefin comprises a linear low-density polyethylene (LLDPE), and the second polyolefin is a bimodal polyethylene comprising the first polyolefin and a high density polyethylene (HDPE).

7. The polyolefin reactor system of claim 1 , wherein the first polyolefin comprises a high density polyethylene (HDPE), and the second polyolefin is a bimodal polyethylene comprising the first polyolefin and a linear low-density polyethylene (LLDPE).

8. The polyolefin reactor system of claim 1 , wherein the polyolefin reactor system is configured to route the recycle stream to the first polymerization reactor or to a recovery system, or both.

9. The polyolefin reactor system of claim 1 , wherein the polyolefin reactor system is configured to route the recycle stream to a suction of a circulation pump of the first polymerization reactor.

10. The polyolefin reactor system of claim 1 , wherein the polyolefin reactor system is configured to add a hydrogenation catalyst to the transfer slurry.

11. A method of operating a polyolefin reactor system, comprising:
polymerizing olefin in the presence of a chain transfer agent in a first reactor to form an intermediate polyolefin;
discharging from the first reactor a transfer slurry comprising the intermediate polyolefin and the chain transfer agent;
processing the transfer slurry to remove chain transfer agent and to provide a fluff slurry comprising the intermediate polyolefin and a lower content of chain transfer agent than in the transfer slurry;
feeding the fluff slurry to a second reactor;
polymerizing olefin in the second reactor to form a product polyolefin; and discharging from the second reactor a product slurry comprising the product polyolefin,
wherein the intermediate polyolefin is continuously transferred from the first reactor, continuously processed to remove chain transfer agent and continuously fed to the second reactor, and
wherein the intermediate polyolefin comprises a linear low-density polyethylene (LLDPE), and the product polyolefin comprises the intermediate polyolefin and a high density polyethylene (HDPE).

12. The method of claim 11 , wherein the product polyolefin is a bimodal polyolefin.

13. The method of claim 11 , wherein the chain transfer agent comprises hydrogen.

14. The method of claim 11 , wherein processing the transfer slurry comprises adding a hydrogenation catalyst to the transfer slurry.

15. The method of claim 11 , wherein processing the transfer slurry comprises reducing pressure of the transfer slurry to flash diluent and the chain transfer agent in the transfer slurry.

16. The method of claim 11 , wherein discharging the transfer slurry from the first reactor comprises discharging continuously the transfer slurry from the first reactor.

17. The method of claim 11 , wherein discharging the transfer slurry from the first reactor comprises discharging the transfer slurry from the first reactor through a settling leg.

18. The method of claim 11 , comprising heating the transfer slurry.

19. A method of operating a polyolefin reactor system, comprising:
polymerizing olefin in the presence of a chain transfer agent in a first reactor to form an intermediate polyolefin;
discharging from the first reactor a transfer slurry comprising the intermediate polyolefin and the chain transfer agent;
processing the transfer slurry to remove chain transfer agent and to provide a fluff slurry comprising the intermediate polyolefin and a lower content of chain transfer agent than in the transfer slurry;
feeding the fluff slurry to a second reactor;
polymerizing olefin in the second reactor to form a product polyolefin; and
discharging from the second reactor a product slurry comprising the product polyolefin,
wherein the intermediate polyolefin is continuously transferred from the first reactor, continuously processed to remove chain transfer agent and continuously fed to the second reactor, and
wherein the intermediate polyolefin comprises a high density polyethylene (HDPE), and the product polyolefin comprises the intermediate polyolefin and a linear low-density polyethylene (LLDPE).

20. A method of operating a polyolefin reactor system, comprising:
polymerizing olefin in the presence of a chain transfer agent in a first reactor to form an intermediate polyolefin;
discharging from the first reactor a transfer slurry comprising the intermediate polyolefin and the chain transfer agent;
processing the transfer slurry to remove chain transfer agent and to provide a fluff slurry comprising the intermediate polyolefin and a lower content of chain transfer agent than in the transfer slurry;
feeding the fluff slurry to a second reactor;
polymerizing olefin in the second reactor to form a product polyolefin; and discharging from the second reactor a product slurry comprising the product polyolefin,
wherein the intermediate polyolefin is continuously transferred from the first reactor, continuously processed to remove chain transfer agent and continuously fed to the second reactor, and
wherein processing the transfer slurry comprises feeding the transfer slurry to a hydrocyclone that removes the chain transfer agent and discharges the fluff slurry.

21. A method of operating a polyolefin reactor system, comprising:
polymerizing olefin in the presence of a chain transfer agent in a first reactor to form an intermediate polyolefin;
discharging from the first reactor a transfer slurry comprising the intermediate polyolefin and the chain transfer agent;
processing the transfer slurry to remove chain transfer agent and to provide a fluff slurry comprising the intermediate polyolefin and a lower content of chain transfer agent than in the transfer slurry;
feeding the fluff slurry to a second reactor;
polymerizing olefin in the second reactor to form a product polyolefin; and discharging from the second reactor a product slurry comprising the product polyolefin,
wherein the intermediate polyolefin is continuously transferred from the first reactor,

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Bhandarkar Maruti
• Benham Elizabeth A
• Gonzales Rebecca A
• Kufeld Scott E
• Mutchler Joel A
• Gill Catherine M
• Nguyen Thanh T
• Odi Timothy O

Classifications

• B01J2219/24

  Stationary reactors without moving elements inside · CPC title

• B01J19/2435 Primary

  Loop-type reactors · CPC title

• B01J19/245

  placed in series · CPC title

• C08F110/02

  Ethene · CPC title

• C08F2/001

  Multistage polymerisation processes characterised by a change in reactor conditions without deactivating the intermediate polymer (C08F295/00, C08F297/00 take precedence) · CPC title