초록 ▼

This invention provides catalyst compositions that are useful for polymerizing at least one monomer to produce a polymer. This invention also provides catalyst compositions that are useful for polymerizing at least one monomer to produce a polymer, wherein said catalyst composition comprises a post-

This invention provides catalyst compositions that are useful for polymerizing at least one monomer to produce a polymer. This invention also provides catalyst compositions that are useful for polymerizing at least one monomer to produce a polymer, wherein said catalyst composition comprises a post-contacted organometal compound, a post-contacted organoaluminum compound, and a post-contacted treated solid oxide compound.

대표청구항 ▼

1. A polymerization process, comprising contacting at least one monomer and a catalyst composition under polymerization conditions to produce a polymer;wherein the catalyst composition is prepared by a process comprising contacting an organometal compound, an organoaluminum compound, and a treated s

1. A polymerization process, comprising contacting at least one monomer and a catalyst composition under polymerization conditions to produce a polymer;wherein the catalyst composition is prepared by a process comprising contacting an organometal compound, an organoaluminum compound, and a treated solid oxide compound to produce the catalyst composition, wherein the organometal compound has the following general formula: (X1)(X2)(X3)(X4)M1 wherein: M1 is selected from titanium, zirconium or hafnium; (X1) is independently selected from cyclopentadienyls, indenyls, fluorenyls, substituted cyclopentadienyls, substituted indenyls, or substituted fluoreyls; substituents on the substituted cyclopentadienyls, substituted indenyls, and substituted fluorenyls of (X1) are selected from aliphatic groups, cyclic groups, combinations of aliphatic and cyclic groups, silyl groups, alkyl halide groups, halides, organometallic groups, phosphorus groups, nitrogen groups, silicon, phosphorus, boron, or germanium; at least one substituent on (X1) can be a bridging group which connects (X1) and (X2); (X3) and (X4) are independently selected from halides, aliphatic groups, substituted aliphatic groups, cyclic groups, substituted cyclic groups, combinations of aliphatic groups and cyclic groups, combinations of substituted aliphatic groups and cyclic groups, combinations of aliphatic groups and substituted cyclic groups, combinations of substituted aliphatic groups and substituted cyclic groups, amido groups, substituted amido groups, phosphido groups, substituted phosphido groups, alkyloxide groups, substituted alkyloxide groups, aryloxide groups, substituted aryloxide groups, organometallic groups, or substituted organometallic groups; (X2) is selected from cyclopentadienyls, indenyls, fluorenyls, substituted cyclopentadienyls, substituted indenyls, substituted fluorenyls, halides, aliphatic groups, substituted aliphatic groups, cyclic groups, substituted cyclic groups, combinations of aliphatic groups and cyclic groups, combinations of substituted aliphatic groups and cyclic groups, combinations of aliphatic groups and substituted cyclic groups, combinations of substituted aliphatic groups and substituted cyclic groups, amido groups, substituted amido groups, phosphido groups, substituted phosphido groups, alkyloxide groups, substituted alkyloxide groups, aryloxide groups, substituted aryloxide groups, organometallic groups, or substituted organometallic groups; substituents on (X2) are selected from aliphatic groups, cyclic groups, combinations of aliphatic groups and cyclic groups, silyl groups, alkyl halide groups, halides, organometallic groups, phosphorus groups, nitrogen groups, silicon, phosphorus, boron, or germanium; and at least one substituent on (X2) can be a bridging group which connects (X1) and (X2); the organoaluminum compound has the following general formula: Al(X5)n(X6)3?n) wherein:(X5) is a hydrocarbyl having from 1 to about 20 carbon atoms; (X6) is a halide, hydride, or alkoxide; and “n” is a number from 1 to 3 inclusive; and the treated solid oxide compound comprises nickel, a halogen, and a solid oxide compound; wherein: the halogen is selected from chlorine or bromine; and the solid oxide compound is selected from alumina, aluminophosphate, aluminosilicate, or mixtures thereof. 2. The polymerization process of claim 1, wherein the polymerization conditions comprise slurry polymerization conditions.3. The polymerization process of claim 2, wherein the polymerization is conducted in a loop reaction zone.4. The polymerization process of claim 3, wherein the polymerization is conducted in the presence of a diluent that comprises isobutane.5. The polymerization process of claim 1, wherein at least one monomer is ethylene.6. The polymerization process of claim 1, wherein at least one monomer comprises ethylene or an aliphatic 1-olefin having 3 to 20 carbon atoms per molecule.7. The polymerization process of claim 1, wherein the catalyst composition has an activity greater than about 1000 grams of polymer per gram of treated solid oxide compound per hour under slurry polymerization conditions, using isobutane as a diluent, with a polymerization temperature of 90° C., and an ethylene pressure of 550 psig.8. The polymerization process of claim 7, wherein the weight ratio of the organoaluminum compound to the treated solid oxide compound in the catalyst composition ranges from about 3:1 to about 1:100.9. The polymerization process of claim 7, wherein the weight ratio of the treated solid oxide compound to the organometal compound in the catalyst composition ranges from about 1000:1 to about 10:1.10. The polymerization process of claim 1, wherein the treated solid oxide compound is calcined at a temperature in a range of about 300° C. to about 800° C., for about 1 hour to about 50 hours.11. The polymerization process of claim 1, wherein the treated solid oxide compound comprises alumina, from about 1 to about 3 millimoles of nickel per gram of alumina, from about 4 to about 20% by weight chlorine, based on the weight of the treated solid oxide compound before calcining.12. The polymerization process of claim 1, wherein the treated solid oxide compound is calcined for about 3 to about 20 hours at a temperature from about 400 to about 700° C., andwherein the treated solid oxide compound comprises alumina, from about 1 to about 3 millimoles of nickel per gram of alumina, and from about 4 to about 20% by weight chlorine, each based on the weight of the treated solid oxide compound before calcining. 13. The polymerization process of claim 1, wherein the organometal compound, the treated solid oxide compound, and the organoaluminum compound are combined by contacting the organometal compound, the treated solid oxide compound, and the organoaluminum compound for about 1 minute to about 1 hour at a temperature from about 15° C. to about 50° C., to form a mixture; and then contacting the mixture with ethylene in a polymerization reaction zone.14. The polymerization process of claim 1, wherein the organometal compound, the organoaluminum compound, and the treated solid oxide compound are precontacted for about 1 minute to about 24 hour at a temperature in a range of about 10° C. to about 200° C.15. The polymerization process of claim 1, wherein the catalyst composition is prepared by a process consisting essentially of contacting the organometal compound, the treated solid oxide compound, and the organoaluminum compound to produce the catalyst composition.16. The polymerization process of claim 15, wherein the treated solid oxide compound is calcined at a temperature in a range of about 300° C. to about 800° C., for about 1 hour to about 50 hours.17. The polymerization process of claim 1, wherein the organometal compound is selected from bis(cyclopentadienyl)hafnium dichloride, bis(cyclopentadienyl)zirconium dichloride, 1,2-ethanediylbis(η5-1-indenyl)di-n-butoxyhafnium, 1,2-ethanediylbis(η5-1-indenyl)dimethylzirconium, 3,3-pentanediylbis(η5-4,5,6,7-tetrahydro-1-indenyl)hafnium dichloride, methylphenylsilylbis(η5-4,5,6,7-tetrahydro-1-indenyl)zirconium dichloride, bis(n-butylcyclopentadienyl)di-t-butylamido hafnium, bis(n-butylcyclopentadienyl)zirconium dichloride; dimethylsilylbis(1-indenyl)zirconium dichloride, nonyl(phenyl)silylbis(1-indenyl)hafnium dichloride, octyl(phenyl)silylbis(1-indenyl)hafnium dichloride, dimethylsilylbis(η5-4,5,6,7-tetrahydro-1-indenyl)zirconium dichloride, dimethylsilylbis(2-methyl-1-indenyl)zirconium dichloride, 1,2-ethanediylbis(9-fluorenyl)zirconium dichloride, indenyl diethoxy titaninm(IV) chloride, (isopropylamidodimethylsilyl)cyclopentadienyltitanium dichloride, bis(pentamethylcyclopentadienyl)zirconium dichloride, bis(indenyl)zirconium dichloride, methyloctylsilylbis(9-fluorenyl)zirconium dichloride, or bis-[1-(N,N-diisopropylamino)boratabenzene]hydridozirconium trifluoromethylsulfonate.18. The polymerization process of claim 17, wherein the organometal compound is selected from bis(n-butylcyclopentadienyl)zirconium dichloride, bis(indenyl)zirconium dichloride, dimethylsilylbis(1-indenyl)zirconium dichloride, or methyloctylsilylbis(9-fluorenyl)zirconium dichloride.19. The polymerization process of claim 1, wherein the halogen is present in an amount in a range of about 2 to about 150% by weight, where the weight percents are based on the weight of the treated solid oxide compound before calcining.20. The polymerization process of claim 1, wherein the nickel is present in an amount in a range of about 0.5 to about 5 millimoles per gram of nickel-containing solid oxide compound before calcining.21. A polymerization process, comprising contacting at least one monomer and a catalyst composition under polymerization conditions to produce a polymer;wherein the catalyst composition is prepared by a process comprising: 1) contacting a solid oxide compound with a nickel-containing compound to produce a nickel-containing solid oxide compound having from about 0.1 to about 10 millimoles of nickel per gram of nickel-containing solid oxide compound before calcining; 2) calcining the nickel-containing solid oxide compound at a temperature within a range of about 200 to about 900° C., for about 1 minute to about 100 hours, to produce a calcined composition; 3) contacting the calcined composition with a halogen-containing compound, after or during calcining, to produce a treated solid oxide compound; 4) combining the treated solid oxide compound with an organometal compound and an organoaluminum compound; wherein the solid oxide compound is selected from alumina, aluminophosphate, aluminosilicate, or mixtures thereof. 22. The polymerization process of claim 21, wherein the organometal compound has the following general formula:(X1)(X2)(X3)(X4)M1 wherein: M2 is selected from titanium, zirconium, or hafnium; (X1) is independently selected from cyclopentadienyls, indenyls, fluorenyls, substituted cyclopentadienyls, substituted indenyls, or substituted fluorenyls; substituents on the substituted cyclopentadienyls, substituted indenyls, and substituted fluorenyls of (X1) are selected from aliphatic groups, cyclic groups, combinations of aliphatic and cyclic groups, silyl groups, alkyl halide groups, halides, organometallic groups, phosphorus groups, nitrogen groups, silicon, phosphorus, boron, or germanium; at least one substituent on (X1) can be a bridging group which connects (X1) and (X2); (X3) and (X4) are independently selected from halides, aliphatic groups, substituted aliphatic groups, cyclic groups, substituted cyclic groups, combinations of aliphatic groups and cyclic groups, combinations of substituted aliphatic groups and cyclic groups, combinations of aliphatic groups and substituted cyclic groups, combinations of substituted aliphatic groups and substituted cyclic groups, amido groups, substituted amido groups, phosphido groups, substituted phosphido groups, alkyloxide groups, substituted alkyloxide groups, aryloxide groups, substituted aryloxide groups, organometallic groups, or substituted organometallic groups; (X2) is selected from cyclopentadienyls, indenyls, fluorenyls, substituted cyclopentadienyls, substituted indenyls, substituted fluorenyls, halides, aliphatic groups, substituted aliphatic groups, cyclic groups, substituted cyclic groups, combinations of aliphatic groups and cyclic groups, combinations of substituted aliphatic groups and cyclic groups, combinations of aliphatic groups and substituted cyclic groups, combinations of substituted aliphatic groups and substituted cyclic groups, amido groups, substituted amido groups, phosphido groups, substituted phosphido groups, alkyloxide groups, substituted alkyloxide groups, aryloxide groups, substituted aryloxide groups, organometallic groups, or substituted organometallic groups; substituents on (X2) are selected from aliphatic groups, cyclic groups, combinations of aliphatic groups and cyclic groups, silyl groups, alkyl halide groups, halides, organometallic groups, phosphorus groups, nitrogen groups, silicon, phosphorus, boron, or germanium; and at least one substituent on (X2) can be a bridging group which connects (X1) and (X2). 23. The polymerization process of claim 21, wherein the organoaluminum compound has the following general formula:Al(X5)n(X6)3?n wherein: (X5) is a hydrocarbyl having from 1 to about 20 carbon atoms; (X6) is a halide, hydride, or alkoxide; and “n” is a number from 1 to 3 inclusive. 24. The polymerization process of claim 21, wherein the nickel-containing compound is nickel nitrate hexahydrate and the organometal compound is bis(n-butylcyclopentadienyl)zirconium dichloride.25. The polymerization process of claim 21, wherein calcined composition is contacted with a halogen-containing compound from about 1 minute to about 10 hours, at a temperature of about 200° C. to about 900° C.26. A polymerization process, comprising contacting at least one monomer and a catalyst composition under polymerization conditions to produce a polymer;wherein the catalyst composition is prepared by a process comprising: 1) contacting alumina with an aqueous solution containing nickel nitrate hexahydrate to produce a nickel-containing alumina having from about 1 to about 3 millimoles of nickel per gram of nickel-containing alumina before calcining; 2) calcining the nickel-containing alumina at a temperature within a range of about 400 to about 700° C., for about 3 to about 20 hours, to produce a calcined composition; 3) contacting the calcined composition with carbon tetrachloride for about 10 minutes to about 30 minutes, to produce a treated solid oxide compound having from about 15 to about 75% by weight chlorine, based on the weight of the treated solid oxide compound before calcining; 4) combining the treated solid oxide compound and bis(n-butylcyclopentadienyl)zirconium dichloride at a temperature within a range of 15° C. to 50° C. to produce a mixture; and 5) combining, after about 1 minute to about 1 hour, the mixture and triethylaluminum to produce the catalyst composition. 27. The polymerization process of claim 26, wherein the process to prepare the catalyst composition consists essentially of steps (1), (2), (3), (4), and (5).