Processes for preparing metallocene-based catalyst systems
US-9493592-B2 · Nov 15, 2016 · US
US9944736B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9944736-B2 |
| Application number | US-201615290010-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 11, 2016 |
| Priority date | Jan 10, 2014 |
| Publication date | Apr 17, 2018 |
| Grant date | Apr 17, 2018 |
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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.
Opening claim text (preview).
We claim: 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
supported on a carrier, e.g. silica, MgCl2, polymer · CPC title
Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond · CPC title
Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title
Monomers containing five or more carbon atoms · CPC title
Melt flow index or melt flow ratio · CPC title
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