Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US10654956B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10654956-B2 |
| Application number | US-201815962522-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 25, 2018 |
| Priority date | May 3, 2017 |
| Publication date | May 19, 2020 |
| Grant date | May 19, 2020 |
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The present disclosure generally relates to ethylene alpha-olefin copolymers and methods of making ethylene alpha-olefin copolymers. The ethylene alpha-olefin copolymers may have a density of about 0.915 g/mL to about 0.918 g/mL, a rheological polydispersity index greater than 0.8, a melt index of about 0.4 dg/10 min to about 2.0 dg/10 min, and/or a CEF T50 of 84° C. or less. The ethylene alpha-olefin copolymers may be made by combining an ethylene monomer and one or more alpha-olefin monomers in the presence of a catalyst, such as a Ziegler-Natta catalyst.
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What is claimed is: 1. An ethylene alpha-olefin copolymer comprising: an ethylene monomer; and an alpha-olefin monomer; wherein the ethylene alpha-olefin copolymer comprises— (i) a density of about 0.915 g/mL to about 0.918 g/mL, (ii) a rheological polydispersity index greater than 0.8, (iii) a melt index of about 0.4 dg/10 min to about 2.0 dg/10 min, and (iv) a CEF T 50 of 84° C. or less. 2. The ethylene alpha-olefin copolymer of claim 1 , wherein the alpha-olefin monomer comprises one or more C 3 -C 10 alpha-olefins. 3. The ethylene alpha-olefin copolymer of claim 2 , wherein the alpha-olefin monomer comprises a C 6 alpha-olefin. 4. The ethylene alpha-olefin copolymer of claim 3 , wherein the C 6 alpha-olefin comprises hex-1-ene. 5. The ethylene alpha-olefin copolymer of claim 1 , wherein the ethylene alpha-olefin copolymer has a density of about 0.915 g/mL to about 0.917 g/mL. 6. The ethylene alpha-olefin copolymer of claim 1 , wherein the ethylene alpha-olefin copolymer has a density of about 0.916 g/mL. 7. The ethylene alpha-olefin copolymer of claim 1 , wherein the ethylene alpha-olefin copolymer has a melt index of about 0.4 dg/10 min to about 1.0 dg/10 min. 8. The ethylene alpha-olefin copolymer of claim 1 , wherein the ethylene alpha-olefin copolymer is film-shaped. 9. A method of producing an ethylene alpha-olefin copolymer comprising: contacting an ethylene monomer and one or more alpha-olefin monomers in the presence of a Ziegler-Natta catalyst to produce the ethylene alpha-olefin copolymer; wherein the ethylene alpha-olefin copolymer has— (i) a density of about 0.915 g/mL to about 0.918 g/mL, (ii) a rheological polydispersity index greater than 0.8, (iii) a melt index of about 0.4 dg/10 min to about 2.0 dg/10 min, and (iv) a CEF T 50 of 84° C. or less. 10. The method of claim 9 , further comprising forming a blown film of the ethylene alpha-olefin copolymer. 11. The method of claim 9 , wherein the Ziegler-Natta catalyst comprises: (i) a compound according to the formula (I)— MR x (I), wherein M is a transition metal of Groups IV to VI of the periodic table, R is a halogen, an alkoxy, or a hydrocarboxyl group, and x is the valence of the transition metal; (ii) a co-catalyst; and (iii) an internal donor (ID) comprising a C 3 -C 6 cyclic ether. 12. The method of claim 11 , wherein the co-catalyst comprises one or more organoaluminum compounds. 13. The method of claim 12 , wherein the co-catalyst comprises trimethylaluminum (TMA). 14. The method of claim 11 , wherein the Ziegler-Natta catalyst further comprises a catalyst support. 15. The method of claim 14 , wherein the catalyst support comprises MgCl 2 . 16. The method of claim 9 , wherein the Ziegler-Natta catalyst comprises: (i) Mg; (ii) Ti; (iii) a halogen; (iv) an electron donor compound; and (v) a co-catalyst; wherein the Ziegler-Natta catalyst has— (a) a molar ratio Mg to Ti of at least 5:1, (b) a molar ratio of Mg to electron donor of less than 2.1:1, and (c) an X-ray diffraction spectrum comprising at least three 2θ diffraction angle peaks between 5.0° and 20.0°, wherein the at least three 2θ diffraction angle peaks comprise a first 2θ diffraction angle peak of 7.2±0.2°, a second 2θ diffraction angle peak of 11.5±0.2°, and a third 2θ diffraction angle peak of 14.5±0.2°, wherein the first 2θ diffraction angle peak of 7.2±0.2° is the most intense and the second 2θ diffraction angle peak of 11.5±0.2° has an intensity less than 0.9 times the intensity of the first 2θdiffraction angle peak. 17. The method of claim 16 , wherein the molar ratio of Mg to electron donor is about 1.1:1 to about 1.4:1. 18. The method of claim 16 , wherein the co-catalyst comprises one or more organoaluminum compounds. 19. The method of claim 18 , wherein the co-catalyst comprises trimethylaluminum (TMA). 20. The method of claim 16 , wherein the electron donor is an inner electron donor.
Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title
inorganic · CPC title
containing magnesium · CPC title
Magnesium halide as support anhydrous or hydrated or complexed by means of a Lewis base for Ziegler-type catalysts · CPC title
Melt flow index or melt flow ratio · CPC title
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