Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US9856339B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9856339-B2 |
| Application number | US-201414911665-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 2, 2014 |
| Priority date | Sep 5, 2013 |
| Publication date | Jan 2, 2018 |
| Grant date | Jan 2, 2018 |
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Methods for making olefin polymerization catalysts and methods for making polyethylene polymers using the catalysts are provided. The polyethylenes can have a molecular weight distribution (MWD) of about 4.5 to about 14, a slope of strain hardening greater than about 0.75, and a melt flow ratio (MFR) greater than or equal to 8.33+(4.17×MWD).
Opening claim text (preview).
What is claimed is: 1. A polyethylene comprising: a molecular weight distribution (MWD) of about 4.5 to about 14; a slope of strain hardening greater than about 0.75, as measured by extensional viscosity fixture (EVF); and wherein the polyethylene has a heterogeneous distribution of short chain branching (SCB) and a melt flow ratio (I 21 /I 2 ) greater than or equal to 8.33+(4.17×MWD). 2. The polyethylene of claim 1 , wherein the polyethylene has a MWD of about 6.8 to about 14. 3. The polyethylene of claim 1 , wherein the polyethylene has a MWD of about 6.9 to about 14. 4. The polyethylene of claim 1 , wherein the polyethylene has a MWD of about 7.0 to about 14. 5. The polyethylene of claim 1 , wherein the polyethylene has a long chain branching (LCB) greater than about 0.01 per 1,000 carbon atoms and less than about 0.07 per 1,000 carbon atoms. 6. The polyethylene of claim 1 , wherein the polyethylene has a long chain branching (LCB) between about 0.05 and 0.06 per 1,000 carbon atoms. 7. The polyethylene of claim 1 , wherein the polyethylene has a long chain branching (LCB) having a length of 4 or more carbon atoms. 8. The polyethylene of claim 1 , wherein the polyethylene has a ratio of weight-average molecular weight calculated using an LS detector to weight-average molecular weight calculated using an RI detector, M w (LS)/M w (RI), of from about 1.4 to about 3.0. 9. The polyethylene of claim 1 , wherein the polyethylene has a ratio of weight-average molecular weight calculated using an LS detector to weight-average molecular weight calculated using an RI detector, M w (LS)/M w (RI), of from about 1.4 to about 2.8. 10. The polyethylene of claim 1 , wherein the polyethylene has a comonomer homogeneity index (CHI) of less than about 0.5. 11. The polyethylene of claim 1 , wherein the polyethylene has a melt flow ratio (I 21 /I 2 ) ranging from about 30 to about 60. 12. The polyethylene of claim 1 , wherein the polyethylene has a melt flow ratio (I 21 /I 2 ) ranging from about 45 to about 60. 13. The polyethylene of claim 1 , wherein the polyethylene has a density of from 0.91 g/cm 3 to about 0.965 g/cm 3 . 14. The polyethylene of claim 1 , wherein the polyethylene has a density greater than or equal to 0.945 g/cm 3 and a melt strength greater than or equal to a ×(3.7463×exp(−1.485×log(MI))), wherein a is equal to 1.5. 15. The polyethylene of claim 1 , wherein the polyethylene has a density greater than or equal to 0.945 g/cm 3 and a melt strength greater than or equal to a ×(3.7463×exp(−1.485×log(MI))), wherein a is equal to 1.75. 16. The polyethylene of claim 1 , wherein the polyethylene has a density greater than or equal to 0.945 g/cm 3 and a melt strength greater than or equal to a ×(3.7463×exp(−1.485×log(MI))), wherein a is equal to 1.9. 17. The polyethylene of claim 1 , wherein the polyethylene has a density less than or equal to 0.945 g/cm 3 and a melt strength greater than or equal to a ×(3.7463×exp(−1.485×log(M1))), wherein a is equal to 1.2. 18. The polyethylene of claim 1 , wherein the polyethylene has a density less than or equal to 0.945 g/cm 3 and a melt strength greater than or equal to a ×(3.7463×exp(−1.485×log(MI))), wherein a is equal to 1.5. 19. The polyethylene of claim 1 , wherein the polyethylene has a density less than or equal to 0.945 g/cm 3 and a melt strength greater than or equal to a ×(3.7463×exp(−1.485×log(MI))), wherein a is equal to 1.9. 20. The polyethylene of claim 1 , wherein the polyethylene is made using a catalyst that is free or essentially free from any electron donors or donor compounds.
Copolymers of ethene (C08J2323/16 takes precedence) · CPC title
Manufacture of films or sheets · CPC title
Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title
and magnesium or compounds thereof · CPC title
Melt flow index or melt flow ratio · CPC title
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