Ethylene polymerization processes and reactor systems for the production of multimodal polymers using combinations of a loop reactor and a fluidized bed reactor

Patent metadata

Field	Value
Publication number	US-11767378-B2
Application number	US-202217934609-A
Country	US
Kind code	B2
Filing date	Sep 23, 2022
Priority date	Feb 1, 2022
Publication date	Sep 26, 2023
Grant date	Sep 26, 2023

Abstract

Polymerization processes and reactor systems for producing multimodal ethylene polymers are disclosed in which at least one loop reactor and at least one fluidized bed reactor are utilized. Configurations include a loop reactor in series with a fluidized bed reactor and two loop reactors in series with a fluidized bed reactor.

First claim

We claim:

1. A polymerization reactor system for producing a multimodal ethylene polymer, the system comprising:
(a) a first loop reactor configured to contact a catalyst composition with ethylene, an optional first olefin comonomer, and optional hydrogen in an inert hydrocarbon diluent under slurry or supercritical polymerization conditions to produce a first ethylene polymer,
wherein the first loop reactor is further configured to maintain a Dean number of from 3,000,000 to 15,000,000 for a reaction mixture flowing through two or more elbow sections in the first loop reactor;
(b) a second loop reactor configured to contact a first reactor effluent containing the first ethylene polymer with ethylene, an optional second olefin comonomer, and optional hydrogen under slurry or supercritical polymerization conditions to produce a second ethylene polymer;
(c) a transfer line configured to withdraw the first reactor effluent containing the first ethylene polymer from the first loop reactor and to introduce the first reactor effluent into the second loop reactor;
(d) a second discharge line configured to withdraw a second reactor effluent containing the second ethylene polymer from the second loop reactor;
(e) a separator configured to remove a light fraction comprising hydrogen from the second reactor effluent to form an intermediate material containing the second ethylene polymer, wherein hydrogen is present in the first loop reactor, the second loop reactor, or both; and
(f) a fluidized bed reactor configured to contact the intermediate material containing the second ethylene polymer with ethylene and an optional third olefin comonomer in an inert gas and/or hydrocarbon under gas phase polymerization conditions to produce the multimodal ethylene polymer;
wherein the transfer line is configured to withdraw the first reactor effluent from the first loop reactor at a discharge location downstream of a first loop reactor circulating pump and to introduce the first reactor effluent into the second loop reactor at a feed location upstream of a second loop reactor circulation pump.

2. The system of claim 1 , wherein the second discharge line is configured to continuously withdraw the second reactor effluent containing the second ethylene polymer from the second loop reactor.

3. The system of claim 1 , wherein an outlet of the separator is positioned at a height greater than that of an inlet of the intermediate material into the fluidized bed reactor.

4. The system of claim 3 , wherein the separator comprises a cyclone.

5. The system of claim 1 , wherein the system further comprises a recycle system configured to separate fine polymer particles from unreacted olefins in a gas stream exiting the fluidized bed reactor, and to convey the fine polymer particles back to the fluidized bed reactor.

6. The system of claim 5 , wherein the recycle system comprises a cyclone and an eductor.

7. The system of claim 1 , wherein the system further comprises a polymer recovery system configured to receive a third reactor effluent containing the multimodal ethylene polymer from the fluidized bed reactor, to remove volatiles from the third reactor effluent, and to form a multimodal ethylene polymer fluff.

8. The system of claim 7 , wherein the polymer recovery system comprises:
a cyclone;
a purge column; and
a continuous fluff discharge between the cyclone and the purge column.

9. A polymerization reactor system for producing a multimodal ethylene polymer, the system comprising:
(a) a loop reactor configured to contact a catalyst composition with ethylene, an optional first olefin comonomer, and hydrogen in an inert hydrocarbon diluent under slurry or supercritical polymerization conditions to produce a first ethylene polymer,
wherein the loop reactor is further configured to maintain a Dean number of from 3,000,000 to 15,000,000 for a reaction mixture flowing through two or more elbow sections in the loop reactor;
(b) a discharge line configured to withdraw a first reactor effluent containing the first ethylene polymer from the loop reactor;
(c) a separator configured to remove a light fraction comprising hydrogen from the first reactor effluent to form an intermediate material containing the first ethylene polymer; and
(d) a fluidized bed reactor configured to contact the intermediate material containing the first ethylene polymer with ethylene and an optional second olefin comonomer in an inert gas and/or hydrocarbon under gas phase polymerization conditions to produce the multimodal ethylene polymer.

10. The system of claim 9 , wherein the separator comprises a cyclone.

11. The system of claim 10 , wherein the cyclone has a cone angle in a range from 60° to 85°.

12. The system of claim 9 , wherein the loop reactor is configured for a linear velocity of a reaction mixture flowing within the loop reactor ranging from 20 to 50 ft/sec.

13. The system of claim 9 , wherein the loop reactor has an inside diameter from 12 to 48 inches.

14. The system of claim 9 , wherein the loop reactor comprises at least reactor circulating pump having an axial design.

15. The system of claim 9 , wherein:
the loop reactor comprises at least reactor circulating pump; and
a diameter of the pump is the same as or greater than an internal diameter of the loop reactor.

16. The system of claim 9 , wherein:
the loop reactor comprises at least reactor circulating pump; and
a diameter of the pump minus an internal diameter of the loop reactor is equal to from 1 to 8 inches.

17. The system of claim 9 , wherein the first reactor effluent is withdrawn continuously from the loop reactor in a continuous take-off assembly.

18. The system of claim 9 , wherein the discharge line further comprises a flashline heater.

19. The system of claim 9 , wherein the system is configured to produce from 20 to 90 wt. % of the multimodal ethylene polymer in the loop reactor and from 10 to 80 wt. % of the multimodal ethylene polymer in the fluidized bed reactor.

20. The system of claim 9 , wherein the system further comprises a control system configured to control a bed height in the fluidized bed reactor.

21. The system of claim 9 , wherein the system further comprises a catalyst feed port configured to introduce the catalyst composition into the loop reactor in a slurry at a solids content of from 1 to 15 wt. %.

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Mutchler Joel A
• Netemeyer Eric J
• Curren Joseph A
• Treptau Michael H
• Dooley Kenneth A
• Lowell Jeffrey S
• Fodor Jeffrey S
• Kufeld Scott E

Classifications

• C08F10/02 Primary

  Ethene · CPC title

• B01J8/24

  according to "fluidised-bed" technique (B01J8/20 takes precedence) · CPC title

• B01J19/1837

  Loop-type reactors · 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

• C08F2/01

  characterised by special features of the polymerisation apparatus used · CPC title