Ethylene copolymer compositions, film and polymerization processes
US-9115233-B2 · Aug 25, 2015 · US
US10370469B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10370469-B2 |
| Application number | US-201715720233-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 29, 2017 |
| Priority date | May 27, 2015 |
| Publication date | Aug 6, 2019 |
| Grant date | Aug 6, 2019 |
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Ethylene/1-butene copolymers made with a single site catalyst system have high melt strength and good processability.
Opening claim text (preview).
What is claimed is: 1. A process for making an ethylene/1-butene copolymer, the process comprising polymerizing ethylene and 1-butene with a single site catalyst system in a gas phase polymerization reactor, wherein the ethylene/1-butene copolymer has density of from 0.912 to 0.94 g/cm 3 , a melt index (12) of from 0.5 to 10 g/10 min, a melt flow ratio (121/12) of from 20 to 35, a molecular weight distribution (M w /M n ) of from 2.0 to 4.5, and an accelerated haul-off melt strength (σ MS ) as determined by Rosand capillary rheometry at 190° C., of at least 3.0 cN; wherein the single site catalyst system comprises a phosphinimine catalyst, a cocatalyst and an inert support. 2. The process of claim 1 wherein the phosphinimine catalyst has the formula: (1-R ¥ -Indenyl)Ti(N═P( t -Bu) 3 )X 2 ; wherein R ¥ is a substituted or unsubstituted alkyl group, a substituted or an unsubstituted aryl group, or a substituted or unsubstituted benzyl group, wherein substituents for the alkyl, aryl or benzyl group are selected from alkyl, aryl, alkoxy, aryloxy, alkylaryl, arylalkyl and halide substituents; and wherein X is an activatable ligand. 3. A process for making an ethylene/1-butene copolymer, the process comprising polymerizing ethylene and 1-butene with a single site catalyst system in a gas phase polymerization reactor, wherein the ethylene/1-butene copolymer has density of from 0.912 to 0.94 g/cm 3 , a melt index (I 2 ) of from 0.5 to 10 g/10 min, a melt flow ratio (I 21 /I 2 ) of from 20 to 35, a molecular weight distribution (M w /M n ) of from 2.0 to 4.5, and which satisfies the following relationship: (CDBI 50 /δ XO ) 3.0 ≤6.5−5.7 log [ a (1.5( I 21 /I 2 )+( M w /M n ))]; where CDBI 50 is the composition distribution breadth index, δ XO is the crossover phase angle at a frequency of 1.0 rad/s and a is the CY a parameter. 4. The process of claim 3 wherein the ethylene/1-butene copolymer further satisfies the relationship: σ MS ≥5.0×10 −4 ×G* XO ; where σ MS is the accelerated haul-off melt strength determined at 190° C.; and G* XO is the crossover complex modulus at a frequency of 1.0 rad/s. 5. The process of claim 3 , wherein the ethylene/1-butene copolymer has an accelerated haul-off melt strength (σ MS ) as determined by Rosand capillary rheometry at 190° C., of at least 3.0 cN. 6. The process of claim 4 , wherein the ethylene/1-butene copolymer has an accelerated haul-off melt strength (σ MS ) as determined by Rosand capillary rheometry at 190° C., of at least 3.0 cN. 7. The process of claim 3 wherein the single site catalyst system comprises a phosphinimine catalyst, a cocatalyst and an inert support. 8. The process of claim 7 wherein the phosphinimine catalyst has the formula: (1-R ¥ -Indenyl)Ti(N═P( t -Bu) 3 )X 2 ; wherein R ¥ is a substituted or unsubstituted alkyl group, a substituted or an unsubstituted aryl group, or a substituted or unsubstituted benzyl group, wherein substituents for the alkyl, aryl or benzyl group are selected from alkyl, aryl, alkoxy, aryloxy, alkylaryl, arylalkyl and halide substituents; and wherein X is an activatable ligand.
containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring · CPC title
Shear ratio or shear ratio index · CPC title
Short chain branches · CPC title
Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title
Copolymers of ethene (C08J2323/16 takes precedence) · CPC title
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