Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US9540460B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9540460-B2 |
| Application number | US-201314765405-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 20, 2013 |
| Priority date | Feb 7, 2013 |
| Publication date | Jan 10, 2017 |
| Grant date | Jan 10, 2017 |
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Catalyst systems and methods for making and using the same are provided. The catalyst systems can include a plurality of silica particles and a metallocene catalyst and an activator supported on the plurality of silica particles. The polymerization catalysts have a particle size distribution in which about 10% of the particles have a size less than about 17 to about 23 micrometers, about 50% of the particles have a size less than about 40 to about 45 micrometers, and about 90% of the particles have a size less than about 72 to about 77 micrometers.
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What is claimed is: 1. A method for forming resin particles, comprising: forming a catalyst compound comprising hafnium; mixing the catalyst compound with an activator to form a catalyst complex; and combining the catalyst complex with a silica support to form a supported polymerization catalyst, wherein the supported polymerization catalyst has a productivity of at least about 7000 g polymer per g catalyst; reacting the supported polymerization catalyst with at least ethylene in a polymerization reactor to form resin particles, wherein the resin particles have: an average polymer particle size of at least about 0.660 mm; a size distribution of at least about 20% greater than 1 mm in diameter; and a ratio of fluidized bulk density to settled bulk density (FBD/SBD) of at least about 0.570. 2. The method of claim 1 , wherein forming the supported polymerization catalyst includes mixing bis(n-propylcyclopentadienyl) hafnium (CH 3 ) 2 with methylaluminoxane to form the catalyst complex; and drying the supported catalyst to bind the catalyst complex to the silica support. 3. The method of claim 1 , further comprising adding a comonomer to the polymerization reactor to control density of the resin particles. 4. The method of claim 1 , wherein the resin particles comprise a polymer having about a 0.7 dg/min MI, about a 0.912 g/cm 3 density, and about a 26 MFR at a temperature of the polymerization reactor of at least about 77° C. 5. The method of claim 1 , wherein the resin particles comprise a polymer having about a 1 dg/min MI, about a 0.918 g/cm 3 density, and about a 28 MFR at a temperature of the polymerization reactor of at least about 75° C. 6. The method of claim 1 , further comprising adding hydrogen to the fluidized bed reactor to control a melt index of the resin particles. 7. The method of claim 1 , wherein the polymerization reactor is a fluidized bed gas phase reactor. 8. The method of claim 1 , further comprising: measuring a sample of the resin particles to obtain an initial product property; and changing a process parameter to obtain a second product property, based, at least in part, on the initial product property. 9. The method of claim 8 , wherein measuring a sample comprises determining a physical property of a plastic sample. 10. The method of claim 8 , wherein measuring a sample comprises determining a physical property of a plastic sample. 11. The method of claim 3 , comprising adjusting a ratio of the comonomer to ethylene within the polymerization reactor to control at least one of the composition distribution, the molecular weight distribution, and the melt index (I 2 ) of a polyethylene. 12. The method of claim 6 , comprising adjusting a ratio of the hydrogen to ethylene within the polymerization reactor to control at least one of the composition distribution, the molecular weight distribution, and the melt index (I 2 ) of a polyethylene.
Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title
Propene · CPC title
Bulk density · CPC title
Monomers containing five or more carbon atoms · CPC title
Monomers containing five or more carbon atoms · CPC title
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