IP Library Granted Patent US 9,303,106
Granted Patent B1
US 9,303,106 · App. 14/517,158 · Granted Apr 5, 2016

Processes for preparing solid metallocene-based catalyst systems

Inventors: Kensha M. Clark (Tulsa, OK); Qing Yang (Bartlesville, OK); Gary L. Glass (Dewey, OK)
Assignee: Chevron Phillips Chemical Company LP
C08F110/02C08F4/6592C08F4/65912C08F4/65916C08F210/16
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Quick Facts
Patent No.
US 9,303,106
App. No.
14/517,158
Granted
Apr 5, 2016
Kind
B1
Abstract

Methods for preparing metallocene-based catalyst systems containing an activator-support are disclosed. These methods can include contacting a solid metallocene compound, an activator-support, and an organoaluminum compound, resulting in catalyst systems with increased catalytic activity as compared to catalyst systems utilizing a solution of the metallocene compound.

Claims (51)

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

(i) contacting an activator-support and a solid metallocene compound for a first period of time to form a precontacted mixture; and

(ii) contacting the precontacted mixture with an organoaluminum compound for a second period of time to produce the catalyst composition;

wherein an activity of the catalyst composition is from about 5% to about 100% greater than that of a catalyst system obtained by using a solution of the metallocene compound instead of the solid metallocene compound, under the same polymerization conditions.

2. The process of claim 1 , wherein in step (i), a slurry of the activator-support in a first diluent is contacted with a slurry of the solid metallocene compound in a second diluent.

3. The process of claim 1 , wherein in step (i), at least one of the activator-support and the solid metallocene compound is a dry solid.

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; and

the solid metallocene compound comprises a bridged zirconium or hafnium based metallocene compound with a cyclopentadienyl group and a fluorenyl group.

5. The process of claim 1 , wherein:

the first period of time is at least about 15 seconds; and

the activity of the catalyst composition is from about 5% to about 75% greater than that of a catalyst system obtained by using a solution of the metallocene compound instead of the solid metallocene compound, under the same polymerization conditions.

6. The process of claim 1 , wherein:

the organoaluminum compound comprises trimethylaluminum, triethylaluminum, tri-n-propylaluminum, tri-n-butylaluminum, triisobutylaluminum, tri-n-hexylaluminum, tri-n-octylaluminum, diisobutylaluminum hydride, diethylaluminum ethoxide, diethylaluminum chloride, or any combination thereof; and

the activator-support comprises fluorided silica-alumina, fluorided silica-coated alumina, sulfated alumina, or a combination thereof.

7. The process of claim 1 , wherein:

a weight ratio of the solid metallocene compound to the activator-support is in a range from about 1:10 to about 1:10,000; and

a weight ratio of the activator-support to the organoaluminum compound is in a range from about 1:5 to about 1000:1.

8. A process to produce a catalyst composition, the process comprising contacting, in any order:

(a) an activator-support;

(b) a solid metallocene compound; and

(c) an organoaluminum compound;

to produce the catalyst composition;

wherein an activity of the catalyst composition is from about 5% to about 100% greater than that of a catalyst system obtained by using a solution of the metallocene compound instead of the solid metallocene compound, under the same polymerization conditions.

9. The process of claim 8 , wherein the process comprises comprising contacting a slurry of the activator-support in a first diluent, a slurry of the solid metallocene compound in a second diluent, and the organoaluminum compound.

10. The process of claim 8 , wherein the process comprises comprising contacting a slurry of the activator-support in a first diluent, a slurry of the solid metallocene compound in a second diluent, and a solution of the organoaluminum compound.

11. The process of claim 8 , wherein at least one of the activator-support and the solid metallocene compound is a dry solid.

12. The process of claim 8 , wherein:

the solid metallocene compound comprises a bridged metallocene compound; and

the activator-support comprises sulfated alumina.

13. The process of claim 8 , wherein:

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

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

the solid 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.

14. The process of claim 8 , wherein the activity of the catalyst composition is from about 5% to about 75% greater than that of a catalyst system obtained by using a solution of the metallocene compound instead of the solid metallocene compound, under the same polymerization conditions.

15. The process of claim 1 , wherein:

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

the solid metallocene compound comprises a bridged zirconium or hafnium based metallocene compound with a cyclopentadienyl group and a fluorenyl group, and with an alkenyl substituent.

16. The process of claim 15 , wherein the activator-support comprises fluorided silica-alumina, fluorided silica-coated alumina, sulfated alumina, or a combination thereof.

17. The process of claim 1 , wherein:

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

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

18. The process of claim 2 , wherein the first diluent and the second diluent independently comprise propane, cyclohexane, isobutane, n-butane, n-pentane, isopentane, neopentane, n-hexane, or combinations thereof.

19. The process of claim 8 , wherein:

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

the solid metallocene compound comprises a bridged zirconium or hafnium based metallocene compound with a cyclopentadienyl group and a fluorenyl group, and with an alkenyl substituent.

20. The process of claim 19 , wherein the activator-support comprises fluorided silica-alumina, fluorided silica-coated alumina, sulfated alumina, or a combination thereof.

21. The process of claim 9 , wherein the first diluent and the second diluent independently comprise propane, cyclohexane, isobutane, n-butane, n-pentane, isopentane, neopentane, n-hexane, or combinations thereof.

22. The process of claim 13 , wherein:

the activator-support comprises fluorided silica-alumina, fluorided silica-coated alumina, sulfated alumina, or a combination thereof; and

the solid metallocene compound comprises an unbridged zirconium based metallocene compound containing a cyclopentadienyl and an indenyl group, and with an alkenyl substituent.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 10, 2014
From: CLARK, KENSHA M.; YANG, QING; GLASS, GARY L.
To: CHEVRON PHILLIPS CHEMICAL COMPANY LP
Reel/Frame 034446/0669 →