IP Library Granted Patent US 9,944,736
Granted Patent B2
US 9,944,736 · App. 15/290,010 · Granted Apr 17, 2018

Processes for preparing metallocene-based catalyst systems

Inventors: Ted H. Cymbaluk (Seabrook, TX); Max P. McDaniel (Bartlesville, OK); Qing Yang (Bartlesville, OK); Dennis L. Holtermann (Conroe, TX)
Assignee: Chevron Phillips Chemical Company LP
C08F210/16C08F4/65904C08F4/65916C08F4/65925C08F4/65927C08F4/52C08F4/65912C08F10/00C08F2500/12
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Quick Facts
Patent No.
US 9,944,736
App. No.
15/290,010
Granted
Apr 17, 2018
Kind
B2
Abstract

Methods for preparing single and dual metallocene catalyst systems containing an activator-support are disclosed. These methods can include precontacting of the activator-support and an organoaluminum compound, as well as sequential contacting of two different metallocene compounds to form a dual metallocene catalyst system.

Claims (66)

1. A process to produce a dual metallocene catalyst composition, the process comprising:

(a) contacting a first metallocene compound and an organoaluminum compound with a slurry of an activator-support for a first period of time to form a first mixture; and

(b) contacting the first mixture with a second metallocene compound for a second period of time to form the dual metallocene catalyst composition;

wherein an activity of the catalyst composition is at least about 10% greater than that of a dual catalyst system obtained by combining the activator-support, a mixture of the first metallocene compound and the second metallocene compound, and the organoaluminum compound, under the same polymerization conditions.

2. The process of claim 1 , wherein:

the first metallocene compound is less reactive with the activator-support than the second metallocene compound; and

a weight ratio of the first metallocene compound to the second metallocene compound is in a range from about 1:10 to about 10:1.

3. The process of claim 1 , wherein:

the activator-support comprises sulfated alumina;

the first metallocene compound comprises a bridged metallocene compound; and

the second metallocene compound comprises an unbridged metallocene compound.

4. The process of claim 1 , wherein:

the activator-support comprises a fluorided solid oxide, a sulfated solid oxide, a phosphated solid oxide, or a combination thereof;

the organoaluminum compound comprises trimethylaluminum, triethylaluminum, tri-n-propylaluminum, tri-n-butylaluminum, triisobutylaluminum, or any combination thereof;

the first metallocene compound comprises a bridged zirconium or hafnium based metallocene compound with a cyclopentadienyl group and a fluorenyl group; and

the second metallocene compound comprises an unbridged zirconium or hafnium based metallocene compound containing two cyclopentadienyl groups, two indenyl groups, or a cyclopentadienyl and an indenyl group.

5. The process of claim 1 , wherein the activity of the catalyst composition is from about 15% to about 100% greater than that of the dual catalyst system obtained by combining the activator-support, the mixture of the first metallocene compound and the second metallocene compound, and the organoaluminum compound, under the same polymerization conditions.

6. An olefin polymerization process, the olefin polymerization process comprising:

(a) contacting a first metallocene compound and an organoaluminum compound with a slurry of an activator-support for a first period of time to form a first mixture;

(b) contacting the first mixture with a second metallocene compound for a second period of time to form the dual metallocene catalyst composition; and

(c) contacting the dual metallocene catalyst composition with an olefin monomer and an optional olefin comonomer in a polymerization reactor system under polymerization conditions to produce an olefin polymer;

wherein a Mw of the olefin polymer produced by the polymerization process is greater than a Mw of an olefin polymer produced under the same polymerization conditions using a dual catalyst system obtained by combining the activator-support, a mixture of the first metallocene compound and the second metallocene compound, and the organoaluminum compound.

7. The olefin polymerization process of claim 6 , wherein:

the polymerization reactor system comprises a slurry reactor, a gas-phase reactor, a solution reactor, or a combination thereof;

the olefin monomer comprises ethylene and the olefin comonomer comprises a C 3 -C 10 alpha-olefin; and

the first metallocene compound produces a higher molecular weight component of the olefin polymer than the second metallocene compound.

8. The olefin polymerization process of claim 7 , wherein:

the olefin polymer comprises a higher molecular weight component and a lower molecular weight component; and

a ratio of the higher molecular weight component to the lower molecular weight component of the olefin polymer produced by the polymerization process is greater than a ratio of the higher molecular weight component to the lower molecular weight component of an olefin polymer produced under the same polymerization conditions using a dual catalyst system obtained by combining the activator-support, a mixture of the first metallocene compound and the second metallocene compound, and the organoaluminum compound.

9. The olefin polymerization process of claim 7 , wherein the catalyst composition is contacted with ethylene and an olefin comonomer comprising 1-butene, 1-hexene, 1-octene, or a mixture thereof.

10. The process of claim 1 , wherein:

the activator-support comprises a sulfated solid oxide and/or a fluorided solid oxide;

the first metallocene compound comprises a bridged metallocene compound and is less reactive with the activator-support than the second metallocene compound; and

the second metallocene compound comprises an unbridged metallocene compound.

11. The process of claim 10 , wherein a weight ratio of the first metallocene compound to the second metallocene compound is in a range from about 1:2 to about 2:1.

12. The olefin polymerization process of claim 6 , wherein:

the dual metallocene catalyst composition is contacted with ethylene and an olefin comonomer comprising a C 3 -C 10 alpha-olefin; and

the first metallocene compound produces a higher molecular weight component of the olefin polymer than the second metallocene compound.

13. The olefin polymerization process of claim 6 , wherein:

the activator-support comprises a fluorided solid oxide, a sulfated solid oxide, a phosphated solid oxide, or a combination thereof; and

the olefin polymer comprises an ethylene homopolymer, an ethylene/1-butene copolymer, an ethylene/1-hexene copolymer, an ethylene/1-octene copolymer, or a combination thereof.

14. The olefin polymerization process of claim 13 , wherein the organoaluminum compound comprises trimethylaluminum, triethylaluminum, tri-n-propylaluminum, tri-n-butylaluminum, triisobutylaluminum, or any combination thereof.

15. The olefin polymerization process of claim 6 , wherein:

the activator-support comprises sulfated alumina;

the first metallocene compound comprises a bridged zirconium or hafnium based metallocene compound with a cyclopentadienyl group and a fluorenyl group; and

the second metallocene compound comprises an unbridged zirconium or hafnium based metallocene compound containing two cyclopentadienyl groups, two indenyl groups, or a cyclopentadienyl and an indenyl group.

16. The olefin polymerization process of claim 6 , wherein:

the first metallocene compound comprises:

 or both; and

the second metallocene compound comprises:

 or both.

17. An olefin polymerization process, the olefin polymerization process comprising:

(a) contacting a first metallocene compound and an organoaluminum compound with a slurry of an activator-support for a first period of time to form a first mixture;

(b) contacting the first mixture with a second metallocene compound for a second period of time to form the dual metallocene catalyst composition; and

(c) contacting the dual metallocene catalyst composition with an olefin monomer and an optional olefin comonomer in a polymerization reactor system under polymerization conditions to produce an olefin polymer; wherein:

the olefin polymer comprises a higher molecular weight component and a lower molecular weight component; and

a ratio of the higher molecular weight component to the lower molecular weight component of the olefin polymer produced by the polymerization process is greater than a ratio of the higher molecular weight component to the lower molecular weight component of an olefin polymer produced under the same polymerization conditions using a dual catalyst system obtained by combining the activator-support, a mixture of the first metallocene compound and the second metallocene compound, and the organoaluminum compound.

18. The olefin polymerization process of claim 17 , wherein:

the first metallocene compound produces the higher molecular weight component of the olefin polymer;

the polymerization reactor system comprises a slurry reactor, a gas-phase reactor, a solution reactor, or a combination thereof; and

the dual metallocene catalyst composition is contacted with ethylene and an olefin comonomer comprising 1-butene, 1-hexene, 1-octene, or a mixture thereof.

19. The olefin polymerization process of claim 18 , wherein the activator-support comprises a fluorided solid oxide, a sulfated solid oxide, a phosphated solid oxide, or a combination thereof.

20. The olefin polymerization process of claim 19 , wherein:

the first metallocene compound comprises a bridged zirconium or hafnium based metallocene compound with a cyclopentadienyl group and a fluorenyl group; and

the second metallocene compound comprises an unbridged zirconium or hafnium based metallocene compound containing two cyclopentadienyl groups, two indenyl groups, or a cyclopentadienyl and an indenyl group.

21. The olefin polymerization process of claim 20 , wherein the organoaluminum compound comprises trimethylaluminum, triethylaluminum, tri-n-propylaluminum, tri-n-butylaluminum, triisobutylaluminum, or any combination thereof.

Continuity (3)
Division 14852692 · Sep 14, 2015
Division 14151848 · Jan 10, 2014
Related Publication 20170029541A1 · Feb 2, 2017