US2012232230A1PendingUtilityA1
Process for making ethylene homopolymers
Individually held — no corporate assignee on recordPriority: Nov 21, 2008Filed: May 16, 2012Published: Sep 13, 2012
Est. expiryNov 21, 2028(~2.3 yrs left)· nominal 20-yr term from priority
Y10S526/903C08F 110/02C08F 10/02B65D 1/0207Y10T428/1397
36
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Claims
Abstract
A process for making an ethylene homopolymer in the presence of an oxide-supported chromium catalyst is disclosed. A small amount of an α-olefin contacted with the catalyst before polymerizing ethylene or introduced into an ethylene homopolymerization unexpectedly boosts process productivity. When used at part per million levels, the α-olefin improves productivity while maintaining desirable polymer properties. The invention is particularly valuable for making HDPE resins useful for blow molding applications.
Claims
exact text as granted — not AI-modified1 - 18 . (canceled)
19 . An article made from an ethylene homopolymer made by a process comprising polymerizing ethylene in a reactor in the presence of an oxide-supported chromium catalyst, a diluent, and an alpha olefin to produce an ethylene homopolymer; wherein the alpha olefin is used in an amount effective to increase the productivity of the process compared with the productivity of the process when performed in the absence of the alpha olefin.
20 . The article of claim 19 comprising a blow molded article.
21 . The article of claim 19 comprising an extruded sheet.
22 . The article of claim 19 comprising an injection molded article.
23 . The article of claim 19 comprising a rotomolded article.
24 . The article of claim 19 comprising an article for wire and cable applications.
25 . The article of claim 19 comprising an article for pipe articles.
26 . The article of claim 19 wherein the reactor is a gas phase process.
27 . The article of claim 19 wherein the reactor is a slurry-loop reactor.
28 . The article of claim 19 wherein the oxide-supported chromium catalyst is contacted with the alpha olefin prior to introducing ethylene into the reactor.
29 . The article of claim 19 wherein the alpha olefin is added to the reactor during the polymerization.
30 . The article of claim 19 wherein the alpha olefin is selected from the group consisting of propylene, 1-butene, isobutylene, and mixtures thereof.
31 . The article of claim 19 wherein the alpha olefin is used in an amount within the range of 1 to 500 ppm based on the amount of diluent.
32 . The article of claim 19 wherein the catalyst further comprises at least one element selected from the group consisting of boron, phosphorus, aluminum, vanadium, titanium, fluorine, and zirconium.
33 . The article of claim 19 wherein the productivity increase is at least 10%.
34 . The article of claim 19 wherein the oxide is selected from the group consisting of silicas, silica-aluminas, aluminas, zirconias, titanias, borias, magnesias, aluminum phosphates, and mixtures thereof.
35 . The article of claim 19 wherein the oxide is a silica.
36 . The article of claim 19 wherein the ethylene homopolymer has a melt index within the range of MI 20 =5 g/10 min. to MI 2 =10 g/10 min., and a density of at least 0.955 g/cm 3 .
37 . An article made from an ethylene homopolymer made by a process comprising polymerizing ethylene in a slurry-loop reactor in the presence of a silica-supported chromium catalyst, a volatile aliphatic hydrocarbon diluent, and an alpha olefin selected from the group consisting of propylene, 1-butene, and isobutylene, to produce an ethylene homopolymer; wherein the alpha olefin is used in an amount within the range of 1 to 500 ppm based on the amount of diluent.
38 . The article of claim 33 comprising a blow molded article.
39 . The article of claim 19 comprising an extruded sheet.Join the waitlist — get patent alerts
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