Preparation of polyolefin

US9540460B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9540460-B2
Application numberUS-201314765405-A
CountryUS
Kind codeB2
Filing dateNov 20, 2013
Priority dateFeb 7, 2013
Publication dateJan 10, 2017
Grant dateJan 10, 2017

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

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.

First claim

Opening claim text (preview).

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.

Assignees

Inventors

Classifications

  • C08F210/16Primary

    Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title

  • Propene · CPC title

  • Bulk density · CPC title

  • C08F10/14Primary

    Monomers containing five or more carbon atoms · CPC title

  • Monomers containing five or more carbon atoms · CPC title

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What does patent US9540460B2 cover?
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…
Who is the assignee on this patent?
Univation Tech Llc
What technology area does this patent fall under?
Primary CPC classification C08F210/16. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Jan 10 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).