Solution process to make ethylene copolymers

US11028192B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11028192-B2
Application numberUS-201816492736-A
CountryUS
Kind codeB2
Filing dateFeb 12, 2018
Priority dateMar 27, 2017
Publication dateJun 8, 2021
Grant dateJun 8, 2021

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  5. First independent claim

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Abstract

Official abstract text for this publication.

This invention relates to a process to polymerize olefins comprising contacting, in solution phase at a temperature of 60° C. to 200° C., ethylene, and at least one olefin comonomer with a catalyst system comprising a non-coordinating anion activator and a metallocene catalyst compound, preferably represented by the formula:and2) obtaining ethylene polymer having an Mw greater than 100,000 g/mol, preferably greater tha 400,000 g/mol.

First claim

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The invention claimed is: 1. A process to polymerize olefins comprising contacting, in solution phase at a temperature of 85° C. to 200° C., ethylene, at least one olefin comonomer, and optional diene, with a catalyst system comprising a non-coordinating anion activator and a metallocene catalyst compound represented by the formula: wherein: M is Hf; each R 3 is independently an anionic group; each R 2 is independently H or a C 1 to C 20 hydrocarbyl or C 1 to C 20 substituted hydrocarbyl; R 4 is a hydrocarbyl radical having from 1 to 20 carbon atoms, hydrides, amides, alkoxides, sulfides, phosphides, halides, dienes, amines, phosphines, ethers, and a combination thereof; R* is phenyl or a substituted phenyl; each R 5 is independently H or a C 1 to C 20 hydrocarbyl or C 1 to C 20 substituted hydrocarbyl; each R 6 is independently H or a C 1 to C 20 hydrocarbyl or C 1 to C 20 substituted hydrocarbyl; each R 7 is independently H or a C 1 to C 20 hydrocarbyl or C 1 to C 20 substituted hydrocarbyl; each R 8 is independently H or a C 1 to C 20 hydrocarbyl or C 1 to C 20 substituted hydrocarbyl; where at least one of each adjacent pair of R 7 and R 8 is not H; and 2) obtaining ethylene copolymer comprising ethylene, from 0.5 to 25 mol % C 3 to C 20 olefin comonomer, and optionally from 0.5 to 20 mol % diene, said ethylene copolymer having a Mw greater than 100,000 g/mol where the % olefin comonomer incorporated is X % or more, where X=(Z−858,441)/(−26,760), where Z is the Mn in g/mol of the ethylene copolymer. 2. The process of claim 1 , wherein R 4 is a C 1 to C 20 hydrocarbyl or C 1 to C 20 substituted hydrocarbyl. 3. The process of claim 1 , wherein R 4 is a C 1 to C 20 alkyl. 4. The process of claim 1 , wherein R 4 and R* are independently a phenyl or a substituted phenyl. 5. The process of claim 1 , wherein R* is alkoxy substituted phenyl, where an alkyl in the alkoxy is a C 1 to C 20 alkyl. 6. The process of claim 1 , wherein each R 6 R 7 and R 8 is independently H or a C 1 to C 20 hydrocarbyl. 7. The process of claim 1 , wherein each R 5 , R 6 , R 7 and R 8 is independently hydrogen, methyl, ethyl, propyl, butyl, pentyl, heptyl, octyl, nonyl, decyl, undecyl, docecyl, or an isomer thereof. 8. The process of claim 1 claim 1 , wherein the catalyst compound comprises: 9. The process of claim 1 , wherein the activator comprises 0 mol % alumoxane. 10. The process of claim 1 , wherein the activator is represented by the formula: where: each R 1 is, independently, a halide; each R 2 is, independently, a halide, a C 6 to C 20 substituted aromatic hydrocarbyl group or a siloxy group of the formula — 0 —Si—R a , where R a is a C 1 to C 20 hydrocarbyl or hydrocarbylsilyl group; each R 3 is a halide, C 6 to C 20 substituted aromatic hydrocarbyl group or a siloxy group of the formula — 0 —Si—R a , where R a is a C 1 to C 20 hydrocarbyl or hydrocarbylsilyl group; L is an neutral Lewis base; (L-H) + is a Bronsted acid; d is 1, 2, or 3, or (L-H) 30 d is (Ar 3 C) 30 d where Ar is substituted or unsubstituted aryl group; wherein the anion has a molecular weight of greater than 1020 g/mol; and wherein at least three of the substituents on the B atom each have a molecular volume of greater than 250 cubic A. 11. The process of claim 10 , wherein (L-H) d 30 is (Ar 3 C) d 30 , where Ar is substituted or unsubstituted aryl group. 12. The process of claim 1 , wherein the activator is one or more of: N,N-dimethylanilinium tetrakis(pentafluorophenyl)borate, triphenylcarbenium tetrakis(pentafluorophenyl)borate, N,N-dimethylanilinium tetrakis(perfluoronaphthyl)borate, N,N-diethylanilinium tetrakis(perfluoronaphthyl)borate, N,N-dimethyl-(2,4,6-trimethylanilinium) tetrakis(perfluoronaphthyl)borate, tropillium tetrakis(perfluoronaphthyl)borate, triphenylcarbenium tetrakis (perfluoronaphthyl)borate, triphenylphosphonium tetrakis(perfluoronaphthyl)borate, triethylsilylium tetrakis(perfluoronaphthyl)borate, N,N-dimethylanilinium tetrakis(perfluorobiphenyl)borate, N,N-diethylanilinium tetrakis(perfluorobiphenyl)borate, N,N-dimethyl-(2,4,6-trimethylanilinium) tetrakis (perfluorobiphenyl)borate, triphenylcarbenium tetrakis(perfluorobiphenyl)borate, triphenylphosphonium tetrakis(perfluorobiphenyl)borate, triethylsilylium tetrakis(perfluorobiphenyl)borate, [4-t-butyl-PhNMe 2 H][(C 6 F 3 (C 6 F 5 ) 2 ) 4 B], triphenylcarbenium tetrakis-(2,3,4,6-tetrafluorophenyl)borate, N,N-dimethylanilinium tetrakis(3,5-bis(trifluoromethyl)phenyl)borate, N,N-diethylanilinium tetrakis(3,5-bis (trifluoromethyl)phenyl)borate, N,N-dimethyl-(2,4,6-trimethylanilinium) tetrakis(3,5-bis (trifluoromethyl)phenyl)borate, tropillium tetrakis(3,5-bis(trifluoromethyl)phenyl)borate, and triphenylcarbenium tetrakis(3,5-bis(trifluoromethyl)phenyl)borate. 13. The process of claim 1 , wherein the process occurs at a temperature of from about 60° C. to about 160° C., at a pressure in the range of from about 0.35 MPa to about 10 MPa, and at a time up to 300 minutes. 14. The process of claim 1 , wherein the comonomer comprises one or more of propylene, butene, pentene, hexene, heptene, octene, nonene, decene, undecene, dodecene, norbornene and isomers thereof. 15. The process of claim 1 , wherein the comonomer comprises propylene. 16. The process of claim 1 , wherein the comonomer comprises propylene and norbornene. 17. The process of claim 1 , wherein the comonomer comprises octene. 18. The process of claim 1 , wherein the comonomer comprises propylene and diene. 19. The process of claim 18 , where the diene is ethylidene norbornene and/or vinyl norbomene. 20. A process to polymerize olefins comprising contacting, in solution phase at a temperature of 85° C. to 200° C., ethylene, diene, and optionally a C 3 to C 20 olefin comonomer, with a catalyst system comprising a non-coordinating anion activator and a metallocene catalyst compound represented by the formula: wherein M is Hf or Zr; each R 3 is independently an anionic group; each R 2 is independently H or a C 1 to C 20 hydrocarbyl or C 1 to C 20 substituted hydrocarbyl; R 4 is a hydrocarbyl radical having from 1 to 20 carbon atoms, hydrides, amides, alkoxides, sulfides, phosphides, halides, dienes, amines, phosphines, ethers, and a combination thereof; R * is phenyl or a substituted phenyl; each R 5 is independently H or a C 1 to C 20 hydrocarbyl or C 1 to C 20 substituted hydrocarbyl; each R 6 is independently H or a C 1 to C 20 hydrocarbyl or C 1 to C 20 substituted hydrocarbyl; each R 7 is independently H or a C 1 to C 20 hydrocarbyl or C 1 to C 20 substituted hydrocarbyl; each R 8 is independently H or a C 1 to C 20 hydrocarbyl or C 1 to C 20 substituted hydrocarbyl; where at least one of each adjacent pair of R 7 and R 8 is not H; and 2) obtaining an ethylene copolymer comprising from 0.5 to 20 mol % diene, optionally from 0.5 to 25 mol % C 3 to C 20 olefin comonomer, and said ethylene copolymer having a Mw greater than 400,000 g/mol, where a % olefin comonomer

Assignees

Inventors

Classifications

  • Heteroatom-substituted bridge, i.e. Cp or analog where the bridge linking the two Cps or analogs is substituted by at least one group that contains a heteroatom · CPC title

  • having one carbon-to-carbon double bond · CPC title

  • in combination with an ionising compound other than alumoxane, e.g. (C6F5)4B-X+ · CPC title

  • C08F10/00Primary

    Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond · CPC title

  • Propene · CPC title

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What does patent US11028192B2 cover?
This invention relates to a process to polymerize olefins comprising contacting, in solution phase at a temperature of 60° C. to 200° C., ethylene, and at least one olefin comonomer with a catalyst system comprising a non-coordinating anion activator and a metallocene catalyst compound, preferably represented by the formula:and2) obtaining ethylene polymer having an Mw greater than 100,000 g/mo…
Who is the assignee on this patent?
Exxonmobil Chemical Patents Inc
What technology area does this patent fall under?
Primary CPC classification C08F10/00. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Jun 08 2021 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 10 related publications on this page (citations in our corpus or others sharing the same primary CPC).