Means for increasing the molecular weight and decreasing the density of ethylene interpolymers employing homogeneous and heterogeneous catalyst formulations

US11111368B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11111368-B2
Application numberUS-202016910141-A
CountryUS
Kind codeB2
Filing dateJun 24, 2020
Priority dateApr 19, 2017
Publication dateSep 7, 2021
Grant dateSep 7, 2021

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  2. Abstract

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Abstract

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A continuous solution polymerization process is disclosed wherein at least two catalyst formulations are employed. A first homogeneous catalyst formulation is employed in a first reactor to produce a first ethylene interpolymer and a first heterogeneous catalyst formulation is employed in a second reactor to produce a second ethylene interpolymer. Optionally a third ethylene interpolymer is formed in a third reactor. The resulting ethylene interpolymer products possess desirable properties in a variety of end use applications, for example in film applications. A means for increasing the molecular weight of the first ethylene interpolymer is disclosed and/or a means for increasing the temperature of the first reactor, relative to a third homogeneous catalyst formulation. A means for reducing the (α-olefin/ethylene) weight ratio in the first reactor is disclosed and/or reducing the density of the first ethylene interpolymer, relative to a third homogeneous catalyst formulation.

First claim

Opening claim text (preview).

What is claimed is: 1. A polyethylene film comprising at least one layer, wherein the layer comprises at least one ethylene interpolymer product comprising: (i) a first ethylene interpolymer; (ii) a second ethylene interpolymer, and; (iii) optionally a third ethylene interpolymer; wherein the ethylene interpolymer product has: a dimensionless Long Chain Branching Factor, LCBF, greater than or equal to about 0.001; from about 0.0015 ppm to about 2.4 ppm of hafnium; has from about 0.1 ppm to about 11.4 ppm of titanium; and has a density from about 0.862 to about 0.975 g/cc; wherein density is measured according to ASTM D792. 2. The polyethylene film according to claim 1 , wherein the ethylene interpolymer product further comprising one or more of the following: (i) greater than or equal to about 0.02 terminal vinyl unsaturations per 100 carbon atoms; (ii) greater than or equal to about 0.12 parts per million (ppm) of a total catalytic metal. 3. The polyethylene film according to claim 1 , wherein the ethylene interpolymer product has a melt index from about 0.3 to about 500 dg/minute; wherein melt index is measured according to ASTM D1238 (2.16 kg load and 190° C.). 4. The polyethylene film according to claim 1 , wherein the ethylene interpolymer product has a M w /M n from about 2 to about 25. 5. The polyethylene film according to claim 1 , wherein the ethylene interpolymer product has a CDBI 50 from about 20% to about 98%. 6. The polyethylene film according to claim 1 , wherein i) the first ethylene interpolymer is from about 5 to about 60 weight percent of the ethylene interpolymer product; (ii) the second ethylene interpolymer is from about 20 to about 95 weight percent of the ethylene interpolymer product, and; (iii) optionally the third ethylene interpolymer is from about 0 to about 30 weight percent of the ethylene interpolymer product; wherein weight percent is the weight of the first, the second or the optional third ethylene interpolymer, individually, divided by the weight of the ethylene interpolymer product. 7. The polyethylene film according to claim 1 , wherein (i) the first ethylene interpolymer has a melt index from about 0.01 to about 200 dg/minute; (ii) the second ethylene interpolymer has melt index from about 0.3 to about 1000 dg/minute, and; (iii) optionally the third ethylene interpolymer has a melt index from about 0.5 to about 2000 dg/minute; wherein melt index is measured according to ASTM D1238 (2.16 kg load and 190° C.). 8. The polyethylene film according to claim 1 , wherein (i) the first ethylene interpolymer has a density from about 0.855 g/cm 3 to about 0.975 g/cc; (ii) the second ethylene interpolymer has a density from about 0.89 g/cm 3 to about 0.975 g/cc, and; (iii) optionally the third ethylene interpolymer has density from about 0.855 g/cm 3 to about 0.975 g/cc; wherein density is measured according to ASTM D792. 9. The polyethylene film according to claim 1 , wherein the ethylene interpolymer product is manufactured using a solution polymerization process. 10. The polyethylene film according to claim 1 , wherein the ethylene interpolymer product further comprises from 0 to about 10 mole percent of one or more α-olefin. 11. The polyethylene film according to claim 10 , wherein the one or more α-olefin are C 3 to C 10 α-olefins. 12. The polyethylene film according to claim 10 , wherein the one or more α-olefin is 1-hexene, 1-octene or a mixture of 1-hexene and 1-octene. 13. The polyethylene film according to claim 1 , wherein the first ethylene interpolymer is produced using at least one homogeneous catalyst formulation. 14. The polyethylene film according to claim 1 , wherein the first ethylene interpolymer is produced using a first homogeneous catalyst formulation. 15. The polyethylene film according to claim 14 , wherein the first homogeneous catalyst formulation is a bridged metallocene catalyst formulation. 16. The polyethylene film according to claim 15 , wherein the bridged metallocene catalyst formulation comprises a component A defined by Formula (I) wherein M is a metal selected from titanium, hafnium and zirconium; G is the element carbon, silicon, germanium, tin or lead; X represents a halogen atom, R 6 groups are independently selected from a hydrogen atom, a C 1-20 hydrocarbyl radical, a C 1-20 alkoxy radical or a C 6-10 aryl oxide radical, these radicals may be linear, branched or cyclic or further substituted with halogen atoms, C 1-10 alkyl radicals, C 1-10 alkoxy radicals, C 6-10 aryl or aryloxy radicals; R 1 represents a hydrogen atom, a C 1-20 hydrocarbyl radical, a C 1-20 alkoxy radical or a C 6-10 aryl oxide radical; R 2 and R 3 are independently selected from a hydrogen atom, a C 1-20 hydrocarbyl radical, a C 1-20 alkoxy radical or a C 6-10 aryl oxide radical, and; R 4 and R 5 are independently selected from a hydrogen atom, a C 1-20 hydrocarbyl radial, a C 1-20 alkoxy radical or a C 6-10 aryl oxide radical. 17. The polyethylene film according to claim 1 , wherein the second ethylene interpolymer is produced using a first heterogeneous catalyst formulation; optionally, the third ethylene interpolymer is produced using the first heterogeneous catalyst formulation or a second heterogeneous catalyst formulation. 18. The polyethylene film according to claim 17 , wherein the first and the second heterogeneous catalyst formulations are a first and a second in-line Ziegler-Natta catalyst formulation; optionally, the first and the second in-line Ziegler-Natta catalyst formulations are the same formulation. 19. The polyethylene film according to claim 17 , wherein the first and the second heterogeneous catalyst formulations are a first and a second batch Ziegler-Natta catalyst formulation; optionally, the first and the second batch Ziegler-Natta catalyst formulations are the same formulation. 20. The polyethylene film according to claim 16 , wherein the third ethylene interpolymer is produced using a fifth homogeneous catalyst formulation. 21. The polyethylene film according to claim 20 , wherein the fifth homogeneous catalyst formulation is the bridged metallocene catalyst formulation, a third homogeneous catalyst formulation or a fourth homogeneous catalyst formulation. 22. The polyethylene film according to claim 21 , wherein the third homogeneous catalyst formulation is an unbridged single site catalyst formulation comprising a component C defined by Formula (II) (L A ) a M(Pl) b (Q) n   (II) wherein M is a metal selected from titanium, hafnium and zirconium; L A is selected from the group consisting of unsubstituted cyclopentadienyl, substituted cyclopentadienyl, unsubstituted indenyl, substituted indenyl, unsubstituted fluorenyl and substituted fluorenyl; Pl is a phosphinimine ligand; Q is independently selected from the group consisting of a hydrogen atom, a halogen atom, a C 1-10 hydrocarbyl radical, a C 1-10 alkoxy radical and a C 5-10 aryl oxide radical; wherein each of the hydrocarbyl, alkoxy, and aryl oxide radicals may be unsubstituted or further substituted by a halogen atom, a C 1-18 alkyl radical, a C 1-8 alkoxy radical, a C 6-10 aryl or aryloxy radical, an amido radical which is unsubstituted or substituted by up to two C 1-8 alkyl radicals or a phosphido radical which is unsubstituted or substituted by up to tw

Assignees

Inventors

Classifications

  • C08F210/16Primary

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

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

  • used for films · CPC title

  • Metallocene or single site catalysts · CPC title

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

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What does patent US11111368B2 cover?
A continuous solution polymerization process is disclosed wherein at least two catalyst formulations are employed. A first homogeneous catalyst formulation is employed in a first reactor to produce a first ethylene interpolymer and a first heterogeneous catalyst formulation is employed in a second reactor to produce a second ethylene interpolymer. Optionally a third ethylene interpolymer is for…
Who is the assignee on this patent?
Nova Chem Int Sa
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 Sep 07 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 6 related publications on this page (citations in our corpus or others sharing the same primary CPC).