Claims
- 1. A catalyst composition for the polymerization or oligomerization of olefins, comprising a metal complex ligated by a monodentate, bidentate, tridentate, or tetradentate ligand, wherein at least one of the donor atoms of the ligand is a nitrogen atom substituted by a 1-pyrrolyl or substituted 1-pyrrolyl group; wherein:
the remaining donor atoms of the ligand are selected from the group consisting of C, N, P, As, O, S, and Se; and wherein
said metal in said metal complex is selected from the group consisting of Sc, Ta, Ti, Zr, Hf, V, Nb, Cr, Mo, W, Mn, Re, Fe, Ru, Os, Co, Rh, Ir, Ni, Cu, Pd, Pt, Al, and Ga.
- 2. A process for the polymerization or oligomerization of olefins, which comprises contacting one or more olefins with the catalyst composition of claim 1.
- 3. The catalyst composition according to claim 1, wherein the metal is selected from the group consisting of Co, Fe, Ni, and Pd, and the ligand is a neutral, bidentate ligand.
- 4. The catalyst according to claim 3, wherein the metal complex is either (i) a compound of formula XIa, or (ii) the reaction product of Ni(1,5-cyclooctadiene)2, B(C6F5)3, one or more olefins, and a neutral bidentate ligand:
- 5. The catalyst according to claim 3, wherein the metal complex is the reaction product of a compound of formula XIb and a second compound Y:
- 6. The catalyst composition according to claims 4 or 5, wherein M is Ni and the neutral bidentate ligand is selected from Set 1:
- 7. The catalyst composition of claims 3, 4, 5, or 6, which is attached to a solid support.
- 8. The catalyst composition according to claim 7, wherein the metal is nickel and the solid support is silica.
- 9. A process for the polymerization or oligomerization of olefins, which comprises contacting one or more olefins with the catalyst composition of claims 3, 4, 5, or 6.
- 10. The process according to claim 9, wherein linear α-olefins are obtained.
- 11. The process according to claim 9, wherein a polyolefin wax is obtained.
- 12. A process for the polymerization of olefins, which comprises contacting one or more olefins with the catalyst composition of claims 7 or 8.
- 13. The process according to claim 12, wherein the metal is Ni, the solid support is silica, and the catalyst is activated by treatment with an alkylaluminum in a gas phase, fluidized bed, olefin polymerization reactor, or in an inlet stream thereof.
- 14. The process according to claim 13, wherein the alkylaluminum is trimethylaluminum.
- 15. A compound selected from Set 2:
- 16. A catalyst composition for the polymerization or oligomerization of olefins, comprising either (i) a cationic Group 8-10 transition metal complex of a neutral bidentate ligand selected from Set 3, or a tautomer thereof, and a weakly coordinating anion X−, or (ii) the reaction product of Ni(1,5-cyclooctadiene)2, B(C6F5)3, one or more olefin monomers, and a neutral bidentate ligand selected from Set 3:
- 17. A process for the polymerization or oligomerization of olefins, which comprises contacting one or more olefins with the catalyst composition of claim 16.
- 18. A ligand selected from Set 4:
- 19. The catalyst composition according to claim 1, wherein M is selected from the group consisting of Co, Ni, and Pd, and the ligand is a monoanionic bidentate ligand.
- 20. The catalyst composition according to claim 19, wherein M is Ni.
- 21. The catalyst according to claim 20, wherein the metal complex is a compound of formula XII:
- 22. The catalyst composition according to claim 21, wherein the monoanionic bidentate ligand is selected from the compounds shown in Set 5, or a tautomer thereof:
- 23. The catalyst composition according to claim 22, which is attached to a solid support.
- 24. A process for the polymerization or oligomerization of olefins, which comprises contacting one or more olefins with the catalyst composition of claim 19.
- 25. The catalyst composition according to claim 1, wherein the metal is selected from the group consisting of Mn, Fe, Ru, and Co, and the ligand is a neutral tridentate ligand.
- 26. The catalyst composition according to claim 25, wherein the metal is Fe or Co.
- 27. The catalyst composition according to claim 26, wherein the metal complex is a compound of formula XIII:
- 28. The catalyst composition according to claim 27, wherein the neutral tridentate ligand is selected from Set 6, or a tautomer thereof:
- 29. The catalyst composition according to claims 25, 26, 27 or 28, which is attached to a solid support.
- 30. The catalyst composition according to claim 29, wherein the solid support is silica.
- 31. A process for the polymerization or oligomerization of olefins, which comprises contacting one or more olefins with the catalyst composition of claims 25, 26, 27, or 28.
- 32. The process according to claim 31, wherein linear α-olefins are obtained.
- 33. The process according to claim 31, wherein a polyolefin wax is obtained.
- 34. A process for the polymerization of olefins, which comprises contacting one or more olefins with the catalyst composition of claims 29 or 30.
- 35. The catalyst composition according to claim 1, wherein the metal is selected from the group Ti, Zr, and Hf, and the ligand is a dianionic bidentate ligand.
- 36. The catalyst composition according to claim 35, wherein the metal complex is a compound of formula XIV:
- 37. The catalyst composition according to claim 36, wherein the dianionic bidentate ligand is selected from Set 7, or a tautomer thereof:
- 38. The catalyst composition according to claim 35, which is attached to a solid support.
- 39. A process for the polymerization of olefins, which comprises contacting one or more olefins with the catalyst composition of claim 35.
- 40. The catalyst composition according to claim 1, wherein the metal is selected from the group consisting of Ti, Zr, and Hf, and the ligand is a monoanionic bidentate ligand.
- 41. The catalyst composition according to claim 40, wherein the metal complex is a compound of formula XV:
- 42. The catalyst composition according to claims 40 or 41, wherein the monoanionic bidentate ligand is selected from Set 8, or a tautomer thereof:
- 43. The catalyst composition according to claim 42, which is attached to a solid support.
- 44. A process for the polymerization of olefins, which comprises contacting one or more olefins with the catalyst composition of claim 40.
- 45. The catalyst composition according to claim 1, wherein the metal is selected from the group consisting of Cr, Mo, and W, and the ligand is a monodentate dianionic ligand.
- 46. The catalyst composition according to claim 45, wherein the metal complex is a compound of formula XVI:
- 47. The catalyst composition according to claim 46, wherein the metal is Cr and the monodentate dianionic ligand is selected from Set 9, or a tautomer thereof:
- 48. The catalyst composition according to claim 47, which is attached to a solid support.
- 49. A process for the polymerization or oligomerization of olefins, which comprises contacting one or more olefins with the catalyst composition of claims 45 or 46.
- 50. The catalyst composition according to claim 1, wherein the metal is selected from the group consisting of V, Nb, and Ta, and the ligand is a monodentate dianionic ligand.
- 51. The catalyst composition according to claim 50, wherein the metal complex is a compound of formula XVII:
- 52. The catalyst composition according to claim 51, wherein the monodentate dianionic ligand is selected from Set 10, or a tautomer thereof, and T1b is a N(hydrocarbyl)2 group:
- 53. The catalyst composition according to claim 52, wherein M is V.
- 54. The catalyst composition according to claims 50, 51, 52 or 53, which is attached to a solid support.
- 55. A process for the polymerization of olefins, which comprises contacting one or more olefins with the catalyst composition of claims 50 or 51.
- 56. The catalyst composition according to claim 1, wherein the metal is selected from the group consisting of Ti, Zr and Hf, and the ligand is a mono- or dianionic ligand comprising a nitrogen donor substituted by a 1-pyrrolyl or substituted 1-pyrrolyl group wherein said nitrogen donor is linked by a bridging group to a cyclopentadienyl, phosphacyclopentadienyl, pentadienyl, 6-oxacyclohexadienyl, or borataaryl group which is also ligated to said metal.
- 57. The catalyst composition according to claim 56, wherein the mono- or dianionic ligand is selected from Set 11, or a tautomer thereof:
- 58. The catalyst composition according to claim 56, wherein said composition is attached to a solid support.
- 59. A process for the polymerization olefins, which comprises contacting one or more olefins with the catalyst composition of claims 56, 57 or 58.
- 60. A process for the polymerization or oligomerization of olefins, comprising contacting a Group 8-10 transition metal catalyst composition with one or more olfins, wherein said catalyst composition exhibits improved thermal stability, wherein said metal complex comprises a bidentate or variable denticity ligand comprising one or two nitrogen donor atom or atoms substituted by an aromatic or heteroaromatic ring, and wherein the ortho positions of said ring are substituted by groups other than H or alkyl; provided that at least one of the ortho positions of at least one of said aromatic or heteroaromatic rings is substituted by an aryl or heteroaryl group.
- 61. A process for the polymerization or oligomerization of olefins, comprising contacting a Group 8-10 transition metal catalyst composition with one or more olefins, wherein said catalyst composition exhibits improved stability in the presence of an amount of hydrogen effective to achieve chain transfer, wherein said metal complex comprises a bidentate or variable denticity ligand comprising one or two nitrogen donor atom or atoms substituted by an aromatic or heteroaromatic ring, and wherein the ortho positions of said ring are substituted by groups other than H or alkyl.
- 62. A process for the polymerization or oligomerization of olefins, comprising contacting a Group 8-10 transition metal catalyst composition with one or more olefins, wherein said catalyst composition exhibits either improved thermal stability, or exhibits improved stability in the presence of an amount of hydrogen effective to achieve chain transfer, or both, wherein said metal complex comprises a bidentate or variable denticity ligand comprising one or two nitrogen donor atom or atoms substituted by an aromatic or heteroaromatic ring, wherein at least one of the ortho positions of at least one of said aromatic or heteroaromatic rings is substituted by an aryl or heteroaryl group which is capable of reversibly forming an agostic bond to said Group 8-10 transition metal under olefin polymerization reaction conditions.
- 63. A process for the polymerization or oligomerization of olefins, comprising contacting a Group 8-10 transition metal catalyst composition with one or more olefins, wherein said catalyst composition exhibits either improved thermal stability, or exhibits improved stability in the presence of an amount of hydrogen effective to achieve chain transfer, or both, wherein said composition comprises a bidentate or variable denticity ligand comprising one or two nitrogen donor atom or atoms substituted by an aromatic or heteroaromatic ring, wherein the ortho positions of said ring are substituted by groups other than H or alkyl; provided that at least one of the ortho positions of at least one of said aromatic or heteroaromatic ring is substituted by an aryl or heteroaryl group.
- 64. The process according to claims 60, 61, 62, or 63, wherein the ortho positions of said ring are substituted by aryl or heteroaryl groups.
- 65. The process according to claims 60, 61, 62, 63, or 64, wherein the half-life for thermal decomposition is greater than 10 min in solution at 60° C., 200 psig ethylene, and the average apparent catalyst activity of said catalyst is greater than 100,000 mol C2H4/mol catalyst/h.
- 66. The process according to claim 65, wherein the half-life for thermal decomposition is greater than 20 minutes, and the average apparent catalyst activity of said catalyst is greater than 1,000,000 mol C2H4/mol catalyst/h.
- 67. The process according to claim 65, wherein the half-life for thermal decomposition of said catalyst is greater than 30 min.
- 68. The process according to claims 60, 61, 62, 63, or 64, wherein the half-life for thermal decomposition is greater than 5 min in solution at 80° C., 200 psig ethylene, and the average apparent catalyst activity of said catalyst is greater than 100,000 mol C2H4/mol catalyst/h.
- 69. The process according to claims 60, 61, 62, 63, or 64, wherein the process temperature is between about 60 and about 150° C.
- 70. The process according to claim 69, wherein the process temperature is between about 100 and about 150° C.
- 71. The process according to claims 60, 61, 62, 63, or 64, wherein the bidentate or variable denticity ligand is selected from Set 12:
- 72. The process according to claim 71, wherein the Group 8-10 transition metal is nickel and the bidentate or variable denticity ligand is selected from Set 13:
- 73. The process according to claim 72, wherein the composition is attached to a solid support.
- 74. The process according to claim 73, wherein the process temperature is between about 60 and about 100° C.
CROSS REFERENCE TO RELATED APPLICATIONS
[0001] This application claims the benefit of the following provisional applications under 35 USC 119, Provisional Application Serial No. 60/121,135, filed Feb. 22, 1999; Provisional Application Serial No. 60/123,385, filed Mar. 8, 1999; Provisional Application Serial No. 60/123,276, filed Mar. 8, 1999; Provisional Application Serial No. 60/130,503, filed Apr. 23, 1999; Provisional Application Serial No. 60/145,277, filed Jul. 26, 1999.
Provisional Applications (5)
|
Number |
Date |
Country |
|
60121135 |
Feb 1999 |
US |
|
60123385 |
Mar 1999 |
US |
|
60123276 |
Mar 1999 |
US |
|
60130503 |
Apr 1999 |
US |
|
60145277 |
Jul 1999 |
US |
Divisions (1)
|
Number |
Date |
Country |
Parent |
09507492 |
Feb 2000 |
US |
Child |
10335995 |
Jan 2003 |
US |