Metallocene and half sandwich dual catalyst systems for producing broad molecular weight distribution polymers

Patent metadata

Field	Value
Publication number	US-9273159-B2
Application number	US-201414493384-A
Country	US
Kind code	B2
Filing date	Sep 23, 2014
Priority date	Sep 25, 2012
Publication date	Mar 1, 2016
Grant date	Mar 1, 2016

Abstract

Disclosed herein are polymerization processes for the production of olefin polymers. These polymerization processes can use a dual catalyst system containing a zirconium or hafnium based metallocene compound and a titanium based half-metallocene compound containing an indenyl group.

First claim

The invention claimed is:

1. A catalyst composition capable of producing an ethylene polymer having a ratio of high load melt index to melt index in a range from about 30 to about 350, the catalyst composition comprising:
catalyst component I comprising a zirconium or hafnium based metallocene compound;
catalyst component II comprising a titanium based half-metallocene compound having formula (IIA):

wherein:
In A is a substituted or unsubstituted indenyl group; and
X 1 , X 2 , and X 3 independently are a monoanionic ligand;

an activator; and
optionally, a co-catalyst.

2. The composition of claim 1 , wherein:
a weight ratio of catalyst component I to catalyst component II is in a range of from about 10:1 to about 1:10;
the catalyst composition comprises only one zirconium or hafnium based metallocene compound, and only one titanium based half-metallocene compound containing an indenyl group; and
the activator comprises an activator-support, the activator-support comprising a solid oxide treated with an electron-withdrawing anion.

3. The composition of claim 1 , wherein the activator comprises an aluminoxane compound, an organoboron or organoborate compound, an ionizing ionic compound, or any combination thereof.

4. The composition of claim 1 , wherein
X 1 , X 2 , and X 3 independently are a halide or C 1 to C 18 hydrocarbyl group.

5. The composition of claim 1 , wherein In A is an unsubstituted indenyl group.

6. The composition of claim 1 , wherein:
each substituent on In A independently is H, a halide, a C 1 to C 36 hydrocarbyl group, a C 1 to C 36 halogenated hydrocarbyl group, a C 1 to C 36 hydrocarboxy group, or a C 1 to C 36 hydrocarbylsilyl group; and
X 1 , X 2 , and X 3 independently are H, BH 4 , a halide, a C 1 to C 36 hydrocarbyl group, a C 1 to C 36 hydrocarboxy group, a C 1 to C 36 hydrocarbylaminyl group, a C 1 to C 36 hydrocarbylsilyl group, a C 1 to C 36 hydrocarbylaminylsilyl group, OBR 1 2 , or OSO 2 R 1 , wherein R 1 is a C 1 to C 36 hydrocarbyl group.

7. The composition of claim 1 , wherein:
each substituent on In A independently is H, Cl, CF 3 , a methyl group, an ethyl group, a propyl group, a butyl group, a pentyl group, a hexyl group, a heptyl group, an octyl group, a nonyl group, a decyl group, an ethenyl group, a propenyl group, a butenyl group, a pentenyl group, a hexenyl group, a heptenyl group, an octenyl group, a nonenyl group, a decenyl group, a phenyl group, a tolyl group, a benzyl group, a naphthyl group, a trimethylsilyl group, a triisopropylsilyl group, a triphenylsilyl group, or an allyldimethylsilyl group; and
X 1 , X 2 , and X 3 independently are a halide or C 1 to C 18 hydrocarbyl group.

8. The composition of claim 1 , wherein catalyst component II comprises:

or any combination thereof.

9. The composition of claim 1 , wherein catalyst component I comprises an unbridged metallocene compound having formula (IA):

wherein:
M is Zr or Hf,
Cp A and Cp B independently are a substituted or unsubstituted cyclopentadienyl or indenyl group; and
X 4 and X 5 independently are a monoanionic ligand.

10. The composition of claim 9 , wherein Cp A and Cp B independently are an unsubstituted cyclopentadienyl or indenyl group.

11. The composition of claim 1 , wherein catalyst component I comprises a bridged metallocene compound having formula (IB):

wherein:
M is Zr or Hf;
Cp C is a substituted cyclopentadienyl, indenyl, or fluorenyl group;
X 4 and X 5 independently are a monoanionic ligand;
R X and R Y independently are H, a halide, a C 1 to C 36 hydrocarbyl group, a C 1 to C 36 halogenated hydrocarbyl group, a C 1 to C 36 hydrocarboxy group, or a C 1 to C 36 hydrocarbylsilyl group; and
E is a bridging group selected from:
a bridging group having the formula >E A R A R B , wherein E A is C or Si, and R A and R B independently are H or a C 1 to C 18 hydrocarbyl group,
a bridging group having the formula —CR C R D —CR E R F -n wherein R C , R D , R E , and R F independently are H or a C 1 to C 18 hydrocarbyl group, or
a bridging group having the formula —SiR G R H —SiR I R J —, wherein R G , R H , R I , and R J independently are H or a C 1 to C 18 hydrocarbyl group.

12. The composition of claim 11 , wherein:
R X and R Y independently are H or a C 1 to C 12 hydrocarbyl group; and
E is a bridging group having the formula >E A R A R B , wherein E A is C or Si, and R A and R B independently are a C 1 to C 12 hydrocarbyl group.

13. A catalyst composition comprising:
catalyst component I comprising a zirconium or hafnium based metallocene compound;
catalyst component II comprising a titanium based half-metallocene compound having formula (IIA):

wherein:
In A is a substituted or unsubstituted indenyl group; and
X 1 , X 2 , and X 3 independently are a monoanionic ligand;

an activator-support; and
optionally, a co-catalyst;
wherein the catalyst composition has an activity of greater than about 100 grams of polyethylene per gram of the activator-support per hour, under slurry polymerization conditions using isobutane as the diluent, at a polymerization temperature of 90° C. and a reactor pressure of 390 psig.

14. The composition of claim 13 , wherein catalyst component I comprises an unbridged zirconium or hafnium based metallocene compound containing two cyclopentadienyl groups, two indenyl groups, or a cyclopentadienyl and an indenyl group.

15. The composition of claim 13 , wherein:
the activator-support comprises fluorided alumina, chlorided alumina, bromided alumina, sulfated alumina, fluorided silica-alumina, chlorided silica-alumina, bromided silica-alumina, sulfated silica-alumina, fluorided silica-zirconia, chlorided silica-zirconia, bromided silica-zirconia, sulfated silica-zirconia, fluorided silica-titania, fluorided silica-coated alumina, sulfated silica-coated alumina, phosphated silica-coated alumina, or any combination thereof; and
the co-catalyst comprises an organoaluminum compound, the organoaluminum compound comprising 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.

16. The composition of claim 13 , wherein:
a weight ratio of catalyst component I to catalyst component II is in a range of from about 4:1 to about 1:4; and
the activator-support comprises fluorided alumina, sulfated alumina, fluorided silica-alumina, sulfated silica-alumina, fluorided silica-coated alumina, sulfated silica-coated alumina, or any combination thereof.

17. The composition of claim 13 , wherein
X 1 , X 2 , and X 3 independently are a halide or a C 1 to C 18 hydrocarbyl group.

18. The composition of claim 17 , wherein:
a weight ratio of catalyst component I to

Assignees

• Chevron Phillips Chemical Co

Inventors

• Ding Errun
• Yang Qing
• Yu Youlu
• Guatney Lloyd W
• Askew Jim B

Classifications

• C08F4/65912 Primary

  in combination with an organoaluminium compound · CPC title

• C08F4/76 Primary

  selected from titanium, zirconium, hafnium, vanadium, niobium or tantalum · CPC title

• C08L23/04

  Homopolymers or copolymers of ethene · CPC title

• C08F4/6592

  containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring · CPC title

• C08F2500/03

  Narrow molecular weight distribution, i.e. Mw/Mn < 3 · CPC title