Method for replacing incompatible ethylene polymerization catalysts

Patent metadata

Field	Value
Publication number	US-9085650-B2
Application number	US-201013514349-A
Country	US
Kind code	B2
Filing date	Dec 17, 2010
Priority date	Dec 18, 2009
Publication date	Jul 21, 2015
Grant date	Jul 21, 2015

Abstract

The present invention relates to a method for optimizing the sequential use of at least two ethylene polymerization catalysts to an ethylene polymerization loop reactor, comprising:
transferring to a mixing vessel a first ethylene polymerization catalyst and a first diluent, thereby providing a first catalyst slurry, transferring said first catalyst slurry from said mixing vessel to an ethylene polymerization loop reactor at a concentration suitable for polymerizing ethylene, increasing the ratio of said diluent to said first ethylene polymerization catalyst in said first catalyst slurry, stopping the supply of said first catalyst slurry to said mixing vessel, stopping the supply of said first catalyst slurry to said ethylene polymerization loop reactor, stopping the supply of ethylene to said ethylene polymerization loop reactor, removing said first catalyst slurry from said ethylene polymerization loop reactor, emptying said mixing vessel, optionally rinsing said mixing vessel with fresh diluent, transferring to said mixing vessel a second ethylene polymerization catalyst and a second diluent, thereby providing a second catalyst slurry, decreasing the ratio of said second diluent to said second ethylene polymerization catalyst in said mixing vessel to obtain a concentration of said second ethylene polymerization catalyst in said second diluent suitable for polymerizing ethylene, transferring said second ethylene polymerization catalyst slurry from said mixing vessel to said ethylene polymerization reactor, restoring the supply of ethylene to said ethylene polymerization loop reactor, restarting ethylene polymerization in said ethylene polymerization loop reactor.

First claim

What is claimed is:

1. A method for optimizing sequential use of at least two ethylene polymerization catalysts in an ethylene polymerization loop reactor, comprising:
transferring to a mixing vessel a first ethylene polymerization catalyst and a first diluent, thereby providing a first catalyst slurry,
transferring said first catalyst slurry from said mixing vessel to an ethylene polymerization loop reactor at a concentration suitable for polymerizing ethylene,
increasing a ratio of said first diluent to said first ethylene polymerization catalyst in said first catalyst slurry,
stopping a supply of said first catalyst slurry to said mixing vessel,
stopping a supply of said first catalyst slurry to said ethylene polymerization loop reactor,
stopping a supply of ethylene to said ethylene polymerization loop reactor,
removing said first catalyst slurry from said ethylene polymerization loop reactor,
emptying said mixing vessel,
optionally rinsing said mixing vessel with fresh diluent,
transferring to said mixing vessel a second ethylene polymerization catalyst and a second diluent, thereby providing a second catalyst slurry,
decreasing a ratio of said second diluent to said second ethylene polymerization catalyst in said mixing vessel to obtain a concentration of said second ethylene polymerization catalyst in said second diluent suitable for polymerizing ethylene,
transferring said second ethylene polymerization catalyst slurry from said mixing vessel to said ethylene polymerization loop reactor,
restoring the supply of ethylene to said ethylene polymerization loop reactor,
restarting ethylene polymerization in said ethylene polymerization loop reactor.

2. The method according to claim 1 , wherein emptying said mixing vessel is performed within a time frame of between 15 minutes to 120 minutes.

3. The method according to claim 2 , wherein said mixing vessel has a capacity of 500 l of diluent.

4. The method according to claim 1 , wherein said first ethylene polymerization catalyst and/or said second ethylene polymerization catalyst is a metallocene catalyst.

5. The method according to claim 1 , wherein said diluent is isobutane.

6. The method according to claim 1 , further comprising the step of rinsing a conduit transferring said first ethylene polymerization catalyst to said mixing vessel with diluent.

7. The method according to claim 1 , further comprising the step of: substantially freeing said ethylene polymerization loop reactor from said first ethylene polymerization catalyst prior to feeding said ethylene polymerization loop reactor with said second ethylene polymerization catalyst.

8. The method according to claim 7 , further comprising the step of: adding a killing agent to said ethylene polymerization loop reactor for removing said first ethylene polymerization catalyst from said ethylene polymerization loop reactor.

9. The method according to claim 8 , wherein said killing agent is selected from a group consisting of water, carbon monoxide and oxygen.

10. The method according to claim 1 , further comprising the step of progressively decreasing ethylene supply to said ethylene polymerization loop reactor.

11. The method according to claim 1 , further comprising the step of intermittently adding ethylene to the ethylene polymerization loop reactor before the second ethylene polymerization catalyst slurry is introduced to said ethylene polymerization loop reactor.

12. The method according to claim 1 , wherein said first ethylene polymerization catalyst is a Ziegler-Natta catalyst, chromium catalyst or a metallocene catalyst.

13. The method according to claim 1 , wherein said second ethylene polymerization catalyst is a Ziegler-Natta catalyst, chromium catalyst or a metallocene catalyst.

14. The method according to claim 1 , wherein said first and said second ethylene polymerization catalysts are incompatible.

15. The method according to claim 1 , wherein said second ethylene polymerization catalyst is for producing in said ethylene polymerization loop reactor a polyethylene with a melt flow index smaller than for a polyethylene obtained in said ethylene polymerization loop reactor with said first ethylene polymerization catalyst.

16. The method according to claim 1 , wherein rinsing said mixing vessel with fresh diluent is abandoned.

Assignees

• Dewachter Daan
• Slawinski Martine
• Total Res & Technology Feluy

Inventors

• Dewachter Daan
• Slawinski Martine

Classifications

• C08F2410/05

  Transitioning, i.e. transition from one catalyst to another with use of a deactivating agent · CPC title

• C08F110/02

  Ethene · CPC title

• C08F10/02 Primary

  Ethene · CPC title

• C08F2/42

  using short-stopping agents · CPC title

• C08F2/01

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