Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US9346896B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9346896-B2 |
| Application number | US-98041510-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 29, 2010 |
| Priority date | Mar 20, 2008 |
| Publication date | May 24, 2016 |
| Grant date | May 24, 2016 |
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Silica-coated alumina activator-supports, and catalyst compositions containing these activator-supports, are disclosed. Methods also are provided for preparing silica-coated alumina activator-supports, for preparing catalyst compositions, and for using the catalyst compositions to polymerize olefins.
Opening claim text (preview).
We claim: 1. A catalyst composition comprising: (a) at least one metallocene compound; and (b) at least one activator-support; wherein the at least one activator-support comprises at least one silica-coated alumina treated with at least one electron-withdrawing anion, wherein: the at least one silica-coated alumina has a weight ratio of alumina to silica in a range from about 1:1 to about 100:1, the at least one electron-withdrawing anion comprises fluoride, and a catalyst activity of the catalyst composition is greater than that of a catalyst system containing the at least one metallocene compound and a silica-alumina treated with the at least one electron-withdrawing anion, under the same polymerization conditions. 2. The catalyst composition of claim 1 , wherein the weight ratio of alumina to silica is in a range from about 2:1 to about 20:1. 3. The catalyst composition of claim 1 , wherein the at least one activator-support comprises at least one silica-coated alumina treated with at least two electron-withdrawing anions, and wherein the at least two electron-withdrawing anions comprise fluoride and phosphate or fluoride and sulfate. 4. The catalyst composition of claim 1 , wherein the at least one silica-coated alumina has a surface area in a range from about 100 to about 1000 m 2 /g, a pore volume greater than about 0.5 mL/g, and a particle size in a range from about 5 microns to about 150 microns. 5. The catalyst composition of claim 1 , wherein the at least one silica-coated alumina is produced by a process comprising: providing at least one alumina source, the at least one alumina source comprising an alumina, a hydrated alumina, aluminum hydroxide, boehmite, or a combination thereof; contacting the at least one alumina source with a solution or suspension comprising at least one solvent and at least one silicon-containing compound capable of producing silica upon calcination; depositing a coating of the at least one silicon-containing compound on at least a portion of the at least one alumina source; and removing the solvent. 6. The catalyst composition of claim 1 , further comprising at least one organoaluminum compound having the formula: Al(X 9 ) m (X 10 ) 3-m ; wherein: X 9 is a hydrocarbyl; X 10 is an alkoxide or an aryloxide, a halide, or a hydride; and m is from 1 to 3, inclusive. 7. The catalyst composition of claim 1 , further comprising at least one optional co-catalyst, wherein the at least one optional co-catalyst is at least one aluminoxane compound, at least one organoboron or organoborate compound, at least one ionizing ionic compound, or any combination thereof. 8. The catalyst composition of claim 1 , further comprising at least one optional activator-support, wherein the at least one optional activator-support is 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, or any combination thereof. 9. The catalyst composition of claim 1 , wherein a catalyst activity of the catalyst composition is greater than about 1000 grams of polyethylene per gram of activator-support per hour under slurry polymerization conditions, using isobutane as a diluent, with a polymerization temperature of 90° C. and a reactor pressure of 420 psig. 10. The catalyst composition of claim 1 , wherein a catalyst activity of the catalyst composition is greater than about 25,000 grams of polyethylene per gram of metallocene compound per hour under slurry polymerization conditions, using isobutane as a diluent, with a polymerization temperature of 90° C. and a reactor pressure of 420 psig. 11. The catalyst composition of claim 1 , wherein the at least one metallocene compound comprises an ansa-metallocene compound. 12. The catalyst composition of claim 1 , wherein the at least one metallocene compound comprises an unbridged metallocene compound. 13. A catalyst composition comprising: (a) at least one metallocene compound; (b) at least one activator-support; and (c) at least one organoaluminum compound; wherein the at least one 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; wherein the at least one activator-support comprises at least one silica-coated alumina treated with at least one electron-withdrawing anion, wherein: the at least one silica-coated alumina has a weight ratio of alumina to silica in a range from about 1.5:1 to about 20:1, the at least one electron-withdrawing anion comprises fluoride, the at least one silica-coated alumina has a surface area in a range from about 250 to about 500 m 2 /g and a pore volume in a range from about 0.8 to about 1.7 mL/g, and a catalyst activity of the catalyst composition is greater than that of a catalyst system containing the at least one metallocene compound, the at least one organoaluminum compound, and a silica-alumina treated with the at least one electron-withdrawing anion, under the same polymerization conditions. 14. The catalyst composition of claim 13 , wherein: the weight ratio of alumina to silica is in a range from about 2:1 to about 12:1. 15. The catalyst composition of claim 14 , wherein the at least one metallocene compound comprises an ansa-metallocene compound. 16. The catalyst composition of claim 11 , further comprising at least one organoaluminum compound. 17. The catalyst composition of claim 16 , wherein the weight ratio of alumina to silica is in a range from about 1.2:1 to about 25:1. 18. The catalyst composition of claim 13 , wherein: the at least one metallocene compound comprises an ansa-metallocene compound.
two cyclopentadienyl rings being mutually non-bridged · CPC title
of aluminium · CPC title
the ligands containing silicon · CPC title
two cyclopentadienyl rings being mutually bridged · CPC title
Ethene · CPC title
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