Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US9714305B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9714305-B2 |
| Application number | US-201414775807-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 21, 2014 |
| Priority date | Mar 15, 2013 |
| Publication date | Jul 25, 2017 |
| Grant date | Jul 25, 2017 |
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Catalyst systems and methods for making and using the same are described herein. A catalyst system can include at least three catalysts. The three catalysts include a metallocene catalyst, a first non-metallocene including a ligand complexed to a metal through two or more nitrogen atoms, and a second non-metallocene including a ligand complexed to a metal through one or more nitrogen atoms and an oxygen atom.
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What is claimed is: 1. A polymerization catalyst system, comprising at least three catalysts, comprising: a metallocene catalyst; a first non-metallocene comprising a ligand complexed to a metal through two or more nitrogen atoms; and a second non-metallocene comprising a catalyst of the formula: or any combinations, wherein X 1 and X 2 are each, independently, phenyl, methyl, chloro, fluoro, or a hydrocarbyl group. 2. The polymerization catalyst system of claim 1 , comprising bis(n-butylcyclopentadienyl) zirconium(X) 2 , wherein each X is, independently, phenyl, methyl, chloro, fluoro, or a hydrocarbyl group. 3. The polymerization catalyst system of claim 1 , comprising bis(n-propylcyclopentadienyl, tetramethylcyclopentadienyl) zirconium(X) 2 , wherein each X is, independently, phenyl, methyl, chloro, fluoro, or a hydrocarbyl group. 4. The polymerization catalyst system of claim 1 , comprising [(pentamethylbenzylNCH 2 ) 2 NH]Zr(X) 2 , wherein each X is, independently, phenyl, methyl, chloro, fluoro, or a hydrocarbyl group. 5. The polymerization catalyst system of claim 1 , comprising a catalyst of the formula: Cp A Cp B MX n or Cp A (A)Cp B MX n , wherein M is a Group 4, 5, or 6 atom; Cp A and Cp B are each bound to M and are independently selected from the group consisting of cyclopentadienyl ligands, substituted cyclopentadienyl ligands, ligands isolobal to cyclopentadienyl and substituted ligands isolobal to cyclopentadienyl; (A) is a divalent bridging group bound to both Cp A and Cp B selected from the group consisting of divalent C 1 to C 20 hydrocarbyls and C 1 to C 20 heteroatom containing hydrocarbonyls, wherein the heteroatom containing hydrocarbonyls comprise from one to three heteroatoms; X is a leaving group selected from the group consisting of chloride ions, bromide ions, C 1 to C 10 alkyls, and C 2 to C 12 alkenyls, carboxylates, acetylacetonates, and alkoxides; and n is an integer from 1 to 3. 6. The polymerization catalyst system of claim 1 , comprising a catalyst of the formula: wherein M is a Group 3 to 12 transition metal or a Group 13 or 14 main group metal; each X is independently an anionic leaving group; y is 0 or 1; n is the oxidation state of M; m is the formal charge of the ligand represented by YZL or YZL′; L is a Group 15 or 16 element; L′ is a group 15 or 16 element or Group 14 containing group; Y is a Group 15 element; Z is a Group 15 element; le and R 2 are independently a C 1 to C 20 hydrocarbon group, a heteroatom containing group having up to twenty carbon atoms, silicon, germanium, tin, lead, or phosphorus; R 1 and R 2 may be interconnected to each other; R 3 is absent, a hydrocarbon group, hydrogen, a halogen, or a heteroatom containing group; R 4 and R 5 are independently an alky group, an aryl group, a substituted aryl group, a cyclic alkyl group, a substituted cyclic alkyl group, a cyclic aralkyl group, a substituted cyclic aralkyl group, or a multiple ring system; R 4 and R 5 may be interconnected to each other; R 6 and R 7 are independently absent, hydrogen, an alkyl group, a halogen, a heteroatom, or a hydrocarbyl group; and R* is absent, hydrogen, a Group 14 atom containing group, a halogen, or a heteroatom containing group. 7. The polymerization catalyst system of claim 1 , wherein the three catalysts are co-supported on a single support. 8. The polymerization catalyst of claim 1 , wherein the first non metallocene catalyst and the second non metallocene catalyst are co-supported on a single support, and at least a portion of the metallocene catalyst is added as a trim feed to the support. 9. The polymerization catalyst system of claim 1 , comprising a slurry mixture.
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