Methods for operating polyethylene reactor systems
US-2024392119-A1 · Nov 28, 2024 · US
US2017145124A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017145124-A1 |
| Application number | US-201715425646-A |
| Country | US |
| Kind code | A1 |
| Filing date | Feb 6, 2017 |
| Priority date | Nov 30, 2011 |
| Publication date | May 25, 2017 |
| Grant date | — |
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A polymer having a long chain branching content peaking at greater than about 20 long chain branches per million carbon atoms, and a polydispersity index of greater than about 10 wherein the long chain branching decreases to approximately zero at the higher molecular weight portion of the molecular weight distribution. A polymer having a long chain branching content peaking at greater than about 8 long chain branches per million carbon atoms, a polydispersity index of greater than about 20 wherein the long chain branching decreases to approximately zero at the higher molecular weight portion of the molecular weight distribution. A polymer having a long chain branching content peaking at greater than about 1 long chain branches per chain, and a polydispersity index of greater than about 10 wherein the long chain branching decreases to approximately zero at the higher molecular weight portion of the molecular weight distribution.
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What is claimed is: 1 . A method of polymerizing C 2 -C 8 monoolefin monomers comprising contacting the monomers with a supported chromium catalyst under conditions suitable for the formation of a polymer, and recovering the polymer; wherein the supported chromium catalyst comprises an alkaline or neutral-aged silica support having a surface area of less than about 250 m 2 /g; and wherein the polymer has a long chain branching content peaking at greater than about 1 long chain branches per chain and a polydispersity index of greater than about 20, wherein the long chain branching decreases to approximately zero at the higher molecular weight portion of the molecular weight distribution. 2 . The method of claim 1 wherein the silica support has a surface area of less than about 200 m 2 /g. 3 . The method of claim 1 wherein the silica support has a surface area of less than about 150 m 2 /g. 4 . The method of claim 1 wherein the silica support has a surface area of less than about 125 m 2 /g. 5 . The method of claim 1 wherein the supported chromium catalyst comprises a chromium distribution of greater than about two chromium atoms per nm 2 of support. 6 . The method of claim 5 wherein supported chromium catalyst further comprises titanium having a distribution of greater than about 2 titanium atoms per nm 2 of support. 7 . The method of claim 6 further comprising an organoaluminum or organoboron cocatalyst. 8 . The method of claim 5 wherein the monomer comprises ethylene and the polymer comprises polyethylene. 9 . The method of claim 8 wherein the long-chain branching content peaks at greater than about 1.3 long-chain branches per chain. 10 . The method of claim 8 wherein the long-chain branching content peaks at greater than about 1.5 long-chain branches per chain. 11 . The method of claim 8 wherein the long-chain branching content peaks at about 20 long chain branches per million carbon atoms. 12 . The method of claim 8 wherein the long-chain branching content peaks at about 20 long chain branches per million carbon atoms. 13 . The method of claim 8 wherein the long-chain branching content peaks at about 25 long chain branches per million carbon atoms. 14 . The method of claim 8 wherein the long-chain branching content peaks at about 30 long chain branches per million carbon atoms. 15 . The method of claim 8 wherein the polymer has a polydispersity index of greater than about 25. 16 . The method of claim 8 wherein the polymer has a density of from about 0.90 g/cc to about 0.97 g/cc. and a melt index of from about 0 dg/min to about 100 dg/min. 17 . A polymer of C 2 -C 8 monoolefin monomers having a long chain branching content peaking at greater than about 1 long chain branches per chain and a polydispersity index of greater than about 20, wherein the long chain branching decreases to approximately zero at the higher molecular weight portion of the molecular weight distribution. 18 . The polymer of claim 17 wherein the long-chain branching content peaks at greater than about 1.3 long-chain branches per chain. 19 . The polymer of claim 17 wherein the long-chain branching content peaks at greater than about 1.5 long-chain branches per chain. 20 . The polymer of claim 18 wherein the long-chain branching content peaks at about 20 long chain branches per million carbon atoms. 21 . The polymer of claim 19 wherein the long-chain branching content peaks at about 20 long chain branches per million carbon atoms. 22 . The polymer of claim 17 wherein the polymer comprises polyethylene having a density of from about 0.90 g/cc to about 0.97 g/cc.
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Long chain branches · CPC title
Broad molecular weight distribution, i.e. Mw/Mn > 6 · CPC title
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