Methods for operating polyethylene reactor systems
US-2024392119-A1 · Nov 28, 2024 · US
US9534711B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9534711-B2 |
| Application number | US-201113881468-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 26, 2011 |
| Priority date | Oct 28, 2010 |
| Publication date | Jan 3, 2017 |
| Grant date | Jan 3, 2017 |
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A single site catalysed ethylene polymer including ethylene and optionally at least one comonomer having a Mw/Mn of less than 5 and wherein the total amount of unsaturations of the ethylene polymer is at least 0.8.
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We claim: 1. A single site catalysed ethylene polymer comprising ethylene and optionally at least one comonomer having a Mw/Mn of less than 5, a density of at least 930 kg/m 3 and wherein the total amount of unsaturations of the ethylene polymer (per average molecule) is at least 0.8. 2. A polymer as claimed in claim 1 having a density of 940 to 955 kg/m 3 . 3. A polymer as claimed in claim 1 having an ethylene content of at least 85 wt %. 4. A polymer as claimed in claim 1 having an MFR 21 of 5 to 50 g/10 min. 5. A polymer as claimed in claim 1 having an Mn value of 25,000 to 75,000. 6. A polymer as claimed in claim 1 having an Mw/Mn of less than 3. 7. A polymer as claimed in claim 1 having carbon-carbon double bonds/1000 carbon atoms in a total amount of at least 0.2/1000 carbon atoms. 8. A polymer as claimed in claim 1 being a homopolymer. 9. A polymer as claimed in claim 1 made using a metallocene catalyst. 10. A polymer as claimed in claim 1 made by a catalyst of formula (I) Cp′ 2 M′X′ 2 wherein each X′ is halogen, C 1-6 alkyl, benzyl or hydrogen; M′ is Hf or Zr; Cp′ is a substituted or unsubstituted cyclopentadienyl or indenyl group. 11. A composition comprising an ethylene polymer as claimed in claim 1 . 12. A process for the preparation of a crosslinked ethylene polymer pipe comprising polymerizing ethylene or ethylene and at least one comonomer in the presence of a single site catalyst to form an ethylene homopolymer or copolymer having a Mw/Mn of less than 5 and wherein the total amount of unsaturations of the ethylene polymer (per average molecule) is at least 0.8 into a pipe by extrusion and crosslinking in the absence of hydrogen. 13. A cross-linked pipe comprising a cross-linked single site catalysed ethylene polymer comprising an ethylene homopolymer or copolymer having a Mw/Mn of less than 5 and wherein the total amount of unsaturations of the ethylene homopolymer or copolymer (per average molecule) is at least 0.8. 14. A pipe as claimed in claim 13 wherein said pipe has a torque max value of at least 7 dNm. 15. A polymer as claimed in claim 10 made by a catalyst of Formula (I) wherein Cp′ is substituted by one or more C 1-10 hydrocarbyl groups. 16. A polymer as claimed in claim 10 made by a catalyst of Formula (I) wherein said Cp′ substituents are bridged. 17. A polymer as claimed in claim 10 made by a catalyst of Formula (I) wherein said Cp′ substituents are bridged with an ethylene or dimethylsilyl link. 18. A process comprising polymerising ethylene or ethylene and at least one comonomer in the presence of a single site catalyst to prepare a single site catalysed ethylene polymer comprising ethylene and optionally at least one comonomer having a Mw/Mn of less than 5, a density of at least 930 kg/m 3 and wherein the total amount of unsaturations of the ethylene polymer (per average molecule) is at least 0.8.
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