Higher density polyolefins with improved stress crack resistance
US-9156970-B2 · Oct 13, 2015 · US
US11512154B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11512154-B2 |
| Application number | US-202217716027-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 8, 2022 |
| Priority date | Dec 8, 2020 |
| Publication date | Nov 29, 2022 |
| Grant date | Nov 29, 2022 |
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Supported chromium catalysts containing a solid oxide and 0.1 to 15 wt. % chromium, in which the solid oxide or the supported chromium catalyst has a particle size span from 0.5 to 1.4, less than 3 wt. % has a particle size greater than 100 μm, and less than 10 wt. % has a particle size less than 10 μm, can be contacted with an olefin monomer in a loop slurry reactor to produce an olefin polymer. Representative ethylene-based polymers produced using the chromium catalysts have a HLMI of 4 to 70 g/10 min, a density from 0.93 to 0.96 g/cm3, from 150 to 680 ppm solid oxide (such as silica), from 1.5 to 6.8 ppm chromium, and a film gel count of less than 15 catalyst particle gels per ft2 of 25 micron thick film and/or a gel count of less than or equal to 50 catalyst particles of greater than 100 μm per five grams of the ethylene polymer.
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We claim: 1. A supported chromium catalyst comprising a solid oxide and from 0.1 to 15 wt. % chromium, wherein the supported chromium catalyst is characterized by: (A1) an amount of the supported chromium catalyst with a particle size greater than 100 μm of less than or equal to 3 wt. %; (A2) a particle size span ((d90−d10)/d50) in a range from 0.5 to 1.4; and (A3) a d10 particle size in a range from 11 to 22 μm. 2. The catalyst of claim 1 , wherein the solid oxide is silica, silica-alumina, silica-coated alumina, silica-titania, silica-titania-magnesia, silica-zirconia, silica-magnesia, silica-boria, aluminophosphate-silica, or any combination thereof. 3. The catalyst of claim 2 , wherein the catalyst comprises from 0.5 to 2 wt. % chromium. 4. The catalyst of claim 3 , wherein the solid oxide is silica and/or silica-titania. 5. The catalyst of claim 1 , wherein the particle size span is from 0.6 to 1.35. 6. The catalyst of claim 1 , wherein the particle size span is from 0.7 to 1.1. 7. The catalyst of claim 1 , wherein the catalyst contains less than or equal to 3 wt. % carbon. 8. The catalyst of claim 1 , wherein at least 80 wt. % of the chromium is present in an oxidation state of three or less. 9. The catalyst of claim 1 , wherein at least 60 wt. % of the chromium is present in an oxidation state of six (Cr+6). 10. The catalyst of claim 1 , wherein the catalyst is further characterized by: a d50 average particle size from 15 to 60 μm; and a ratio of d80/d20 from 1.3 to 2.8. 11. The catalyst of claim 1 , wherein the catalyst is further characterized by: a d50 average particle size from 17 to 32 μm; and a d95 particle size from 30 to 55 μm. 12. The catalyst of claim 1 , wherein less than or equal to 1 wt. % of the supported chromium catalyst has a particle size greater than 100 μm. 13. The catalyst of claim 1 , wherein: the solid oxide is silica, silica-alumina, silica-coated alumina, silica-titania, silica-titania-magnesia, silica-zirconia, silica-magnesia, silica-boria, aluminophosphate-silica, or any combination thereof; and at least 80 wt. % of the chromium is present in an oxidation state of three or less. 14. The catalyst of claim 13 , wherein the catalyst is further characterized by: a d50 average particle size from 15 to 60 μm; and a ratio of d80/d20 from 1.3 to 2.8. 15. The catalyst of claim 13 , wherein the particle size span is from 0.6 to 1.35. 16. The catalyst of claim 13 , wherein: the catalyst comprises from 0.5 to 2 wt. % chromium; and the solid oxide is silica, silica-coated alumina, or silica-titania. 17. The catalyst of claim 16 , wherein: less than or equal to 1 wt. % of the supported chromium catalyst has a particle size greater than 100 μm; and less than or equal to 3 wt. % of the supported chromium catalyst has a particle size less than 10 μm. 18. The catalyst of claim 16 , wherein the particle size span is from 0.7 to 1.1. 19. The catalyst of claim 16 , wherein the catalyst is further characterized by: a d50 average particle size from 17 to 32 μm; and a d95 particle size from 30 to 55 μm. 20. The catalyst of claim 16 , wherein the catalyst contains, independently, less than 0.1 ppm of Mg, V, Ti, Zr, or Hf. 21. The catalyst of claim 1 , wherein: the solid oxide is silica, silica-alumina, silica-coated alumina, silica-titania, silica-titania-magnesia, silica-zirconia, silica-magnesia, silica-boria, aluminophosphate-silica, or any combination thereof; and at least 60 wt. % of the chromium is present in an oxidation state of six (Cr+6). 22. The catalyst of claim 21 , wherein the catalyst is further characterized by: a d50 average particle size from 15 to 60 μm; and a ratio of d80/d20 from 1.3 to 2.8. 23. The catalyst of claim 21 , wherein the particle size span is from 0.6 to 1.35. 24. The catalyst of claim 21 , wherein: the catalyst comprises from 0.5 to 2 wt. % chromium; and the solid oxide is silica, silica-coated alumina, or silica-titania. 25. The catalyst of claim 24 , wherein: less than or equal to 1 wt. % of the supported chromium catalyst has a particle size greater than 100 μm; and less than or equal to 3 wt. % of the supported chromium catalyst has a particle size less than 10 μm. 26. The catalyst of claim 24 , wherein the particle size span is from 0.7 to 1.1. 27. The catalyst of claim 24 , wherein the catalyst is further characterized by: a d50 average particle size from 17 to 32 μm; and a d95 particle size from 30 to 55 μm. 28. The catalyst of claim 24 , wherein the catalyst contains, independently, less than 0.1 ppm of Mg, V, Ti, Zr, or Hf.
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