Higher Density Polyolefins With Improved Stress Crack Resistance

US2016304644A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2016304644-A1
Application numberUS-201615193195-A
CountryUS
Kind codeA1
Filing dateJun 27, 2016
Priority dateSep 5, 2013
Publication dateOct 20, 2016
Grant date

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  1. Title

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Abstract

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Disclosed herein are polymerization processes for the production of olefin polymers. These polymerization processes can employ a catalyst system containing two or three metallocene components, resulting in ethylene-based copolymers that can have a medium density and improved stress crack resistance.

First claim

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1 - 14 . (canceled) 15 . A catalyst composition comprising: catalyst component I comprising an unbridged Group IV transition metal based metallocene compound; catalyst component II comprising a bridged Group IV transition metal based metallocene compound with a fluorenyl group; catalyst component III comprising a titanium or chromium half-metallocene compound; an activator; and optionally, a co-catalyst. 16 . The composition of claim 15 , wherein the activator comprises an aluminoxane compound, an organoboron or organoborate compound, an ionizing ionic compound, or any combination thereof. 17 . An olefin polymerization process, the process comprising contacting the catalyst composition of claim 15 with an olefin monomer and an optional olefin comonomer in a polymerization reactor system under polymerization conditions to produce an olefin polymer, wherein the catalyst composition comprises: an unbridged metallocene compound containing two cyclopentadienyl groups, two indenyl groups, or a cyclopentadienyl and an indenyl group; a bridged metallocene compound with a cyclopentadienyl group and fluorenyl group, and an alkenyl substituent on the cyclopentadienyl group and/or on the bridging group; a half-metallocene compound having formula (IIIA) or formula (IIIB): wherein: Ind is an indenyl group; Cp C is a cyclopentadienyl, indenyl, or fluorenyl group; each X independently is a monoanionic ligand; and each L is a neutral ligand, and integer n is 0, 1 or 2; an activator-support comprising a solid oxide treated with an electron-withdrawing anion; and an organoaluminum compound. 18 . The process of claim 17 , wherein: the activator-support comprises a fluorided solid oxide and/or a sulfated solid oxide; the 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; catalyst component I comprises an unbridged metallocene compound having formula (I) and catalyst component II comprises a bridged metallocene compound having formula (II): each M independently is Zr or Hf; Cp A and Cp B independently are a cyclopentadienyl or indenyl group; Cp is a cyclopentadienyl group; each X independently is a monoanionic ligand; R X and R Y independently are H, a halide, a C 1 to C 36 hydrocarbyl group, a C 1 to C 36 halogenated hydrocarbyl group, a C 1 to C 36 hydrocarboxy group, or a C 1 to C 36 hydrocarbylsilyl group; and E is a bridging group. 19 . The process of claim 17 , wherein the polymerization reactor system comprises a slurry reactor, gas-phase reactor, solution reactor, or a combination thereof. 20 . The process of claim 17 , wherein the catalyst composition is contacted with ethylene and an olefin comonomer comprising 1-butene, 1-hexene, 1-octene, or a mixture thereof. 21 . The composition of claim 15 , wherein: the catalyst composition comprises a co-catalyst; catalyst component I comprises an unbridged zirconium based metallocene compound containing two cyclopentadienyl groups, two indenyl groups, or a cyclopentadienyl and an indenyl group; and catalyst component II comprises a bridged zirconium or hafnium based metallocene compound with a cyclopentadienyl group and a fluorenyl group. 22 . The composition of claim 21 , wherein: a weight ratio of catalyst component Ito catalyst component II is from about 10:1 to about 1:10; and a weight percentage of catalyst component III is in a range from about 5 to about 50 wt. %, based on the total weight of catalyst components I, II, and III. 23 . The composition of claim 22 , wherein catalyst component III has formula (IIIA): wherein: Ind is an indenyl group; and each X independently is a monoanionic ligand. 24 . The composition of claim 23 , wherein: Ind is an unsubstituted indenyl group or a mono-substituted indenyl group; and each X is Cl. 25 . The composition of claim 22 , wherein catalyst component III has formula (IIIB): Cr(Cp C )(X)(X)(L) n   (IIIB); wherein: Cp C is a cyclopentadienyl, indenyl, or fluorenyl group; each X independently is a monoanionic ligand; and each L is a neutral ligand, and integer n is 0, 1 or 2. 26 . The composition of claim 25 , wherein: Cp C is a cyclopentadienyl group; each X independently is a halide or a C 1 to C 18 hydrocarbyl group; and n is equal to 0 or 1. 27 . The composition of claim 21 , wherein: a weight ratio of catalyst component Ito catalyst component II is from about 5:1 to about 1:5; and a weight percentage of catalyst component III is in a range from about 10 to about 45 wt. %, based on the total weight of catalyst components I, II, and III. 28 . The composition of claim 21 , wherein the activator comprises an aluminoxane compound, an organoboron or organoborate compound, an ionizing ionic compound, or any combination thereof. 29 . The composition of claim 21 , wherein: the activator comprises a fluorided solid oxide and/or a sulfated solid oxide; and the co-catalyst comprises an organoaluminum compound. 30 . The composition of claim 29 , wherein the 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; 31 . The process of claim 20 , wherein catalyst component I comprises an unbridged zirconium based metallocene compound containing two indenyl groups. 32 . The process of claim 20 , wherein catalyst component I comprises an unbridged zirconium based metallocene compound containing a cyclopentadienyl and an indenyl group. 33 . The process of claim 20 , wherein the half-metallocene compound has formula (IIIA). wherein each X is Cl. 34 . The process of claim 20 , wherein the half-metallocene compound has formula (IIIB): Cr(Cp C )(X)(X)(L) n   (IIIB); wherein: Cp C is a cyclopentadienyl group; each X independently is a monoanionic ligand; and L is a neutral ligand, and integer n is 0 or 1.

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Classifications

  • two cyclopentadienyl rings being mutually bridged · CPC title

  • with aliphatic 1-olefins containing one carbon-to-carbon double bond · CPC title

  • in combination with an organoaluminium compound · CPC title

  • Copolymers of ethene (C08J2323/16 takes precedence) · CPC title

  • two cyclopentadienyl rings being mutually non-bridged · CPC title

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What does patent US2016304644A1 cover?
Disclosed herein are polymerization processes for the production of olefin polymers. These polymerization processes can employ a catalyst system containing two or three metallocene components, resulting in ethylene-based copolymers that can have a medium density and improved stress crack resistance.
Who is the assignee on this patent?
Chevron Phillips Chemical Co Lp
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 Thu Oct 20 2016 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). 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).