Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US9416206B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9416206-B2 |
| Application number | US-201113005388-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 12, 2011 |
| Priority date | Jan 22, 2010 |
| Publication date | Aug 16, 2016 |
| Grant date | Aug 16, 2016 |
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Provided are ethylene propylene copolymers compositions thereof and methods for making the same. The composition may include an ethylene copolymer, comprising 40 wt % to 70 wt % of units derived from ethylene, and at least 30 wt % of units derived from at least one α-olefin having 3 to 20 carbon atoms. The composition can have a melting point (Tm) in ° C., as measured by DSC, that satisfies the relation: Tm>3.4×E−180, where E is the weight % of units derived from ethylene in the copolymer. The composition can also have a Mw/Mn ratio of about 1.5 to about 3.5. The composition can further have a content of Group 4 metals derived from a catalyst of 25 ppm or less.
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What is claimed is: 1. A composition comprising an ethylene-propylene copolymer, which copolymer was prepared in a single reactor using a single catalyst system, comprising 40 wt % to 65 wt % of units derived from ethylene, and at least 35 wt % of units derived from propylene, wherein the composition has: 40-65 wt % units derived from ethylene; a melting point (Tm) in ° C., as measured by DSC, that satisfies the relation: Tm>3.4 ×E −180 where E is the weight % of units derived from ethylene in the ethylene-propylene copolymer; a Mw/Mn ratio of about 1.5 to about 3.5; and a content of Group 4 metals derived from a catalyst of 25 ppm or less. 2. The composition of claim 1 , wherein the ethylene-propylene copolymer has a weight-average molecular weight (Mw), as measured by GPC, of about 50,000 g/mol to about 200,000 g/mol. 3. The composition of claim 1 , wherein the composition has a shear stability index, SSI, and a thickening efficiency, TE, satisfying the relation: TE>0.034*SSI+0.8. 4. The composition of claim 1 , wherein the composition has a pour point of about −35° C. or less. 5. The composition of claim 1 , wherein the composition has a low temperature viscosity in a Mini Rotary Viscometer (MRV) test at −25° C. of about 20,000 cP or less. 6. The composition of claim 1 , wherein the composition has a shear stability index, SSI, of about 35% to about 50%. 7. The composition of claim 1 , wherein the ethylene-propylene copolymer has a ratio of wt ppm Group 4 metals derived from a catalyst to wt ppm Group 5 metals derived from a catalyst of at least 3. 8. A lubricating oil composition, comprising: a base oil; and a high SSI viscosity index improver comprising an ethylene-propylene copolymer, which copolymer was prepared in a single reactor using a single catalyst system, comprising 40 wt % to 65 wt % of units derived from ethylene; and at least 35 wt % of units derived from propylene, wherein the ethylene-propylene copolymer has: a melting point (Tm) in ° C., as measured by DSC, that satisfies the relation: Tm>3.4 ×E −180 where E is the weight % of units derived from ethylene in the ethylene-propylene copolymer; a ratio of Mw/Mn of about 1.5 to about 3.5; and a content of Group 4 metals derived from a catalyst of 25 ppm or less; and further wherein the high SSI viscosity index improver has 40 wt % to 65 wt % units derived from ethylene. 9. The lubricating oil composition of claim 8 , wherein the ethylene-propylene copolymer has a weight-average molecular weight (Mw), as measured by GPC, of about 50,000 g/mol to about 200,000 g/mol. 10. The lubricating oil composition of claim 8 , wherein the lubricating oil composition has a shear stability index, SSI, and a thickening efficiency, TE, satisfying the relation: TE>0.034*SSI+0.8. 11. The lubricating oil composition of claim 8 , wherein the lubricating oil composition has a pour point of about −35° C. or less. 12. The lubricating oil composition of claim 8 , wherein the lubricating oil composition has a low temperature viscosity in a Mini Rotary Viscometer (MRV) test at −25° C. of about 20,000 cP or less. 13. The lubricating oil composition of claim 8 , wherein the lubricating oil composition has a shear stability index, SSI, of about 35% to about 50%. 14. The lubricating oil composition of claim 8 , wherein the ethylene-propylene copolymer has a ratio of wt ppm Group 4 metals derived from a catalyst to wt ppm Group 5 metals derived from a catalyst of at least 3. 15. A lubricating oil composition, comprising: a base oil and a high SSI viscosity index improver comprising an ethylene-propylene copolymer, which copolymer was prepared in a single reactor using a single catalyst system, comprising 40 wt % to 65 wt % of units derived from ethylene and at least 12 wt % of units derived from propylene, wherein the ethylene-propylene copolymer has: a weight-average molecular weight (Mw), as measured by GPC, in the range of about 50,000 to about 200,000 g/mol; a melting point (Tm), as measured by DSC, of at least 100° C.; a ratio of Mw/Mn of about 1.5 to about 3.5; and a content of Group 4 metals derived from a catalyst of 25 ppm or less; and further wherein the high SSI viscosity index improver has 40 wt % to 65 wt % units derived from ethylene. 16. The lubricating oil composition of claim 15 , wherein the ethylene-propylene copolymer further comprises a shear stability index, SSI, and a thickening efficiency, TE, satisfying the relation: TE>0.034*SSI+0.08. 17. The lubricating oil composition of claim 15 , wherein the lubricating oil composition has a pour point of about −40° C. or less. 18. The lubricating oil composition of claim 15 , wherein the lubricating oil composition has a shear stability index, SSI, of about 35% to about 50%. 19. The lubricating oil composition of claim 15 , wherein the ethylene-propylene copolymer has a ratio of wt ppm Group 4 metals derived from a catalyst to wt ppm Group 5 metals derived from a catalyst of at least 3. 20. A method for making a lubricating oil composition, comprising: reacting ethylene and propylene in a single reactor in the presence of a single catalyst system at conditions sufficient to produce a high SSI viscosity index improver comprising an ethylene-propylene copolymer, said high SSI viscosity index improver having 40 wt % to 65 wt % of units derived from ethylene, wherein the single catalyst system consists of a dimethylsilyl(bisindenyl) hafnium dimethyl metallocene and a trimethylammonium tetrakis-pentafluorophenylborate activator; and wherein the ethylene-propylene copolymer has: 40 wt % to 65 wt % of units derived from ethylene and at least 35 wt % of units derived from propylene; a weight-average molecular weight (Mw), as measured by GPC, in the range of about 50,000 to about 200,000 g/mol; a melting point (Tm), as measured by DSC, that satisfies the relation: Tm>3.4 ×E −180 where E is the weight % of units derived from ethylene in the ethylene-propylene copolymer; a ratio of Mw/Mn of about 1.5 to about 3.5; and a content of Group 4 metals derived from a catalyst of 25 ppm or less; and blending the high SSI viscosity index improver with a base oil in an amount sufficient to produce a lubricating oil composition. 21. The method of claim 20 , wherein the ethylene-propylene copolymer has a ratio of wt ppm Group 4 metals derived from a catalyst to wt ppm Group 5 metals derived from a catalyst of at least 3. 22. The method of claim 20 , wherein the ethylene-propylene copolymer has a weight-average molecular weight (Mw), as measured by GPC, of about 50,000 g/mol to about 200,000 g/mol. 23. The method of claim 20 , wherein the ethylene-propylene copolymer has a shear stability index, SSI, and a thickening efficiency, TE, satisfying the relation: TE>0.034*SSI+0.8. 24. The method of claim 20 , wherein the ethylene-propylene copolymer has a pour point of about −35° C. or less. 25. A lubricating oil composition comprising the composition of claim 1 .
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