Methods for operating polyethylene reactor systems
US-2024392119-A1 · Nov 28, 2024 · US
US12540206B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12540206-B2 |
| Application number | US-202118021408-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 27, 2021 |
| Priority date | Sep 30, 2020 |
| Publication date | Feb 3, 2026 |
| Grant date | Feb 3, 2026 |
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The present inventions concerns a copolymer of ethylene and an C3 to C8 alpha-olefin, wherein the copolymer has a density of 870 to 890 kg/m 3 measured according to ISO 1183, a MFR 2 of 0.5 to 8.0 g/10 min measured according to ISO 1133, wherein the alpha-olefin is present in the copolymer in an amount of 20 to 35 wt.-%, wherein the copolymer has a first melting temperature T m1 measured according to ISO 11357-3, characterized in that the first melt point T m1 is between 90 and 115° C.
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The invention claimed is: 1 . Copolymer of ethylene and an C3 to C8 alpha-olefin, wherein the copolymer has a density of 870 to 890 kg/m 3 measured according to ISO 1183, a MFR 2 of 0.5 to 8.0 g/10 min measured according to ISO 1133, wherein the alpha-olefin is present in the copolymer in an amount of 20 to 35 wt. %, wherein the copolymer has a first melting temperature T m1 measured according to ISO 11357-3, characterized in that the first melt temperature T m1 is between 9° and 110° C.; and in that the copolymer has a second melting temperature T m2 measured according to ISO 11357-3, wherein the second melting temperature T m2 is between 35 and 55° C. 2 . The copolymer according to claim 1 , wherein the copolymer is a copolymer of ethylene and octene. 3 . The copolymer according to claim 1 , wherein the copolymer has a MFR 2 of 0.7 to 4.0 g/10 min measured according to ISO 1133. 4 . The copolymer according to claim 1 , wherein the copolymer has an MFR 21 of 25 to 50 g/10 min measured according to ISO 1133. 5 . The copolymer according to claim 1 , wherein the copolymer has a ratio MFR 21 /MFR 2 of 25 to 40 measured according to ISO 1133. 6 . The copolymer according to claim 1 , wherein the copolymer has an Mw/Mn of 2.6 to 3.3 determined by Gel Permeation Chromatography. 7 . The copolymer according to claim 1 , wherein the copolymer has an Mw of 85000 to 100000 g/mol determined by Gel Permeation Chromatography. 8 . The copolymer according to claim 1 , wherein the copolymer has a glass transition temperature T g of −45 to −60° C. measured according to ISO 6721-7. 9 . The copolymer according to claim 1 , wherein the copolymer has a vinyl content of 3.5 to 6.5 vinyl groups per 100000 carbon atoms measured with ′H NMR. 10 . The copolymer according to claim 1 , wherein the copolymer has a vinylidene content of 10.0 to 20.0 vinylidene groups per 100000 carbon atoms measured with 1 H NMR. 11 . The copolymer according to claim 1 , wherein the copolymer has a trisubstituted vinylene content of 16.0 to 27.0 trisubstituted vinylene groups per 100000 carbon atoms measured with 1 H NMR. 12 . The copolymer according to claim 1 , wherein the copolymer has a vinylene content of 7.0 to 14.0 vinylene groups per 100000 carbon atoms measured with 1 H NMR. 13 . The copolymer according to claim 1 , wherein the copolymer is obtained by blending a first ethylene copolymer and a second ethylene copolymer, wherein the first ethylene copolymer has a higher density than the second ethylene copolymer. 14 . The copolymer according to claim 13 , wherein a blending ratio of the first ethylene copolymer to the second ethylene copolymer is from 25:75 to 55:45 wt. %.
with aliphatic 1-olefins containing one carbon-to-carbon double bond · CPC title
Ethene · CPC title
Internal unsaturations · CPC title
Amount of comonomer in wt% or mol% · CPC title
Glass transition temperature [Tg] · CPC title
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