Methods for operating polyethylene reactor systems
US-2024392119-A1 · Nov 28, 2024 · US
US9428636B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9428636-B2 |
| Application number | US-201214001209-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 1, 2012 |
| Priority date | Mar 28, 2011 |
| Publication date | Aug 30, 2016 |
| Grant date | Aug 30, 2016 |
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An ethylene/α-olefin copolymer comprising units derived from ethylene; and units derived from at least one α-olefin; wherein the ethylene/α-olefin copolymer has a density in the range of from 0.90 to 0.94 g/cc; a melt index (I 2 ) in the range of from 0.05 to 50 dg/min; an Mw/Mn of from 3 to 5; and from 300 to 500 vinyl unsaturations per 1,000,000 carbon atoms in the ethylene/α-olefin copolymer is provided. Also provided is a process for producing an ethylene/α-olefin copolymer comprising: (1) polymerizing ethylene and one or more α-olefins in a polymerization reactor; (2) thereby producing an enhanced melt strength ethylene/α-olefin copolymer having from 300 to 500 vinyl unsaturation units per 1,000,000 carbon atoms, a density in the range of from 0.90 to 0.94 g/cc; a melt index (I 2 ) in the range of from 0.05 to 50 dg/min; and a Mw/Mn of from 3 to 5.
Opening claim text (preview).
We claim: 1. A blend comprising: an ethylene/1-octene copolymer comprising units derived from ethylene and units derived from 1-octene, wherein the ethylene/1-octene copolymer has a density in the range of from 0.921 to 0.94 g/cc; a melt index (I 2 ) in the range of 0.05 to 50 dg/min; an Mw/Mn of from 3 to 5; and from 300 to 350 vinyl unsaturations per 1,000,000 carbon atoms in the ethylene/1-octene copolymer; and wherein the ethylene/1-octene copolymer is produced using a polymerization step occurring at a temperature of at least 205° C.; and a low density polyethylene (LDPE). 2. The blend according to claim 1 , wherein the ethylene/1-octene copolymer has a melt strength of at least 3.0 cN. 3. The blend according to claim 1 , wherein the ethylene/1-octene copolymer has from 330 to 350 vinyl unsaturations per 1,000,000 carbon atoms in the ethylene/1-octene copolymer. 4. A film comprising the blend according to claim 1 . 5. A process for producing an ethylene/1-octene copolymer comprising: polymerizing ethylene and 1-octene in a polymerization reactor, wherein the ethylene/1-octene copolymer is produced using a polymerization step occurring at a temperature of at least 205° C., thereby producing an ethylene/1-octene copolymer having a density in the range of from 0.921 to 0.94 g/cc; a melt index (I 2 ) in the range of 0.05 to 50 dg/min; an Mw/Mn of from 3 to 5; and from 300 to 350 vinyl unsaturations per 1,000,000 carbon atoms in the ethylene/1-octene copolymer. 6. The process of claim 5 , wherein the polymerization step occurs in the presence of 0.01 to 0.04 mole percent of hydrogen. 7. The process of claim 5 , wherein the polymerization step occurs in the presence of 0.015 to 0.03 mole percent of hydrogen. 8. The process of claim 5 , wherein the polymerization step occurs at a temperature from 205 to 240° C. 9. The process of claim 5 , wherein the polymerization step occurs at a temperature from 205 to 215° C. 10. The process of claim 5 , wherein the polymerization step occurs in a single stage solution reactor. 11. The process of claim 5 , further comprising adding, post-reactor, a primary antioxidant to a product stream produced in the polymerization step. 12. The process of claim 5 , further comprising adding, post-reactor, a secondary antioxidant to a product stream produced in the polymerization step. 13. The process of claim 12 , wherein the secondary antioxidant is a phosphite.
with aliphatic 1-olefins containing one carbon-to-carbon double bond · CPC title
Pre-melted polymers · CPC title
Copolymers of ethene (C08J2323/16 takes precedence) · CPC title
having four to nine carbon atoms · CPC title
Phosphorus bound to oxygen only · CPC title
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