IP Library › Granted Patent US 8,609,791
Granted Patent B2
US 8,609,791 · App. 13/514,101 · Granted Dec 17, 2013

Method for replacing compatible ethylene polymerization catalysts

Inventors: Daan Dewachter (Mechelen, BE); Martine Slawinski (Nivelles, BE)
Assignee: Total Research & Technology Feluy
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Quick Facts
Patent No.
US 8,609,791
App. No.
13/514,101
Granted
Dec 17, 2013
Kind
B2
Abstract

The present invention relates to a method for optimizing the sequential feeding of at least two ethylene polymerization catalysts to an ethylene polymerization reactor, comprising: transferring to a mixing vessel a first ethylene polymerization catalyst and a first diluent, decreasing the concentration of said first ethylene polymerization catalyst in said mixing vessel, transferring to said mixing vessel a second ethylene polymerization catalyst and a second diluent, progressively replacing said first ethylene polymerization catalyst by said second ethylene polymerization catalyst and said first diluent by said second diluent, increasing the concentration of said second ethylene polymerization catalyst in said mixing vessel, sequentially transferring said first ethylene polymerization catalyst and said second ethylene polymerization catalyst from said mixing vessel to an ethylene polymerization reactor.

Claims (33)

1. Method for optimizing the sequential feeding of at least two ethylene polymerization catalysts to an ethylene polymerization reactor, comprising:

transferring to a mixing vessel a first ethylene polymerization catalyst and a first diluent,

decreasing the concentration of said first ethylene polymerization catalyst in said mixing vessel,

transferring to said mixing vessel a second ethylene polymerization catalyst and a second diluent,

progressively replacing said first ethylene polymerization catalyst by said second ethylene polymerization catalyst and said first diluent by said second diluent,

increasing the concentration of said second ethylene polymerization catalyst in said mixing vessel,

sequentially transferring said first ethylene polymerization catalyst and said second ethylene polymerization catalyst from said mixing vessel to an ethylene polymerization reactor.

2. Method according to claim 1 , whereby said first diluent is the same as said second diluent.

3. Method according to claim 1 , whereby increasing or decreasing a concentration is obtained by raising or lowering of said first diluent or said second diluent transferred to said mixing vessel.

4. Method according to claim 1 , whereby decreasing said concentration of said first ethylene polymerization catalyst in said mixing vessel, is obtained by increasing the relative amount of said first diluent to said first ethylene polymerization catalyst in said mixing vessel.

5. Method according to claim 1 , whereby increasing said concentration of said second ethylene polymerization catalyst in said mixing vessel, is obtained by lowering the relative amount of said second diluent to said second ethylene polymerization catalyst in said mixing vessel.

6. Method according to claim 1 , whereby sequentially transferring said first ethylene polymerization catalyst and said second ethylene polymerization catalyst is providing said ethylene polymerization reactor with a catalyst concentration suitable for the production of polyethylene when producing said polyethylene.

7. Method according to claim 1 , whereby said first and/or said second diluent is injected into a conduit for transferring said first ethylene polymerization catalyst and/or said second ethylene polymerization catalyst to said mixing vessel.

8. Method according to claim 1 , whereby said first ethylene polymerization catalyst is replaced by said second ethylene polymerization catalyst upon reaching a pre-set catalyst concentration in said mixing vessel suitable for polymerizing ethylene.

9. Method according to claim 8 , whereby said pre-set catalyst concentration is a catalyst concentration, expressed per weight of diluent in said mixing vessel, of between 0.05 and 2.9 weight percent.

10. Method according to claim 9 , further comprising the step of lowering ethylene in said ethylene polymerization reactor prior to progressively replacing said first ethylene polymerization catalyst by said second ethylene polymerization catalyst.

11. Method according to claim 10 , further comprising the step of: transferring said first ethylene polymerization catalyst and/or said second ethylene polymerization catalyst from said mixing vessel to said ethylene polymerization reactor at a flow rate adjusted to said ethylene.

12. Method according to claim 10 , whereby said ethylene is lowered by at least two percent.

13. Method according to claim 1 , further comprising the step of: lowering hydrogen and/or co-monomer in said ethylene polymerization reactor.

14. Method according to claim 1 , whereby said first ethylene polymerization catalysts and said second ethylene polymerization catalyst are selected from a list consisting of a metallocene catalyst, a Ziegler-Natta catalyst and a chromium catalyst, and whereby said first ethylene polymerization catalyst is different from said second ethylene polymerization catalyst.

15. Method according to claim 1 , whereby said first ethylene polymerization catalyst is replaced by said second ethylene polymerization catalyst within at most 2 hours.

16. Method according to claim 1 , whereby the first diluent comprises isobutane.

17. Method according to claim 6 , wherein the ethylene polymerization reactor is a double loop reactor.

18. Method according to claim 6 , wherein the polyethylene is bimodal polyethylene.

19. Method according to claim 9 , wherein the catalyst concentration, expressed per weight of diluent in said mixing vessel, is between 0.1 and 0.3 weight percent.

20. Method according to claim 9 , wherein the catalyst concentration, expressed per weight of diluent in said mixing vessel, is 0.2 weight percent.

21. Method according to claim 12 , whereby the ethylene is lowered by at least 5 percent.

22. Method according to claim 12 , whereby the ethylene is lowered by at most 10 percent.

23. Method according to claim 14 , whereby either the first ethylene polymerization catalysts or the second ethylene polymerization catalyst is a single site catalyst.

24. Method according to claim 14 , whereby either the first ethylene polymerization catalysts or the second ethylene polymerization catalyst is a metallocene catalyst.

25. Method according to claim 14 , whereby either the first ethylene polymerization catalysts or the second ethylene polymerization catalyst is a carrier supported metallocene catalyst.

26. Method according to claim 15 , whereby the first ethylene polymerization catalyst is replaced by the second ethylene polymerization catalyst within at most 1.5 hours.

27. Method according to claim 15 , whereby the first ethylene polymerization catalyst is replaced by the second ethylene polymerization catalyst within at most 1 hour.

Assignments (2)
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNOR NAME: DEWACHTER, DANN PREVIOUSLY RECORDED ON REEL 029454 FRAME 0197. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNOR NAME: DEWACHTER, DAAN. Recorded Feb 26, 2013
From: DEWACHTER, DAAN; SLAWINSKI, MARTINE
To: TOTAL RESEARCH & TECHNOLOGY FELUY
Reel/Frame 029874/0491 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 12, 2012
From: DEWACHTER, DANN; SLAWINSKI, MARTINE
To: TOTAL RESEARCH & TECHNOLOGY FELUY
Reel/Frame 029454/0197 →
Priority Claims (1)
EP 09179864 · Dec 18, 2009 · regional
Continuity (1)
Related Publication 20120252989A1 · Oct 4, 2012