Claims
- 1. A process of preparing a polymer composition that includes a branched crystalline diene-modified polypropylene random terpolymer, comprising:
contacting a metallocene catalyst compound with a polymerization medium that includes at least a propylene monomer, a first diene monomer, and a second diene monomer, in which the first diene monomer and the second diene monomer are different non-conjugated dienes, each having 5 or more carbon atoms; and conducting polymerization of the monomers in the presence of the metallocene catalyst compound for a time sufficient to provide a branched crystalline diene-modified polypropylene random terpolymer that includes monomeric units derived from each of the monomers, and having from 0.0 wt % to 2.0 wt % ethylene and a heat of fusion of 30 J/g or more.
- 2. A process of preparing a polymer composition that includes a branched crystalline diene-modified polypropylene random terpolymer, comprising:
contacting a metallocene catalyst compound with a polymerization medium that includes at least a propylene monomer, an α, internal non-conjugated diene monomer, and a α, ω non-conjugated diene monomer; and conducting polymerization of the monomers in the presence of the metallocene catalyst compound for a time sufficient to provide a branched crystalline diene-modified polypropylene random terpolymer that includes monomeric units derived from each of the monomers, and having from 0.0 wt % to 2.0 wt % ethylene and a heat of fusion of 30 J/g or more.
- 3. The process of claim 1, in which the first diene monomer is an α, internal diene.
- 4. The process of claim 1, in which the second diene monomer is an α, ω diene.
- 5. The process of claim 1, in which the first diene monomer is an α, internal non-conjugated diene monomer; and the second diene monomer is an α, ω non-conjugated diene monomer.
- 6. The process of claim 1, in which either the first diene monomer or the second diene monomer has an internal double bond comprising a disubstituted vinyl group or a tri-substituted vinyl group.
- 7. The process of claim 1, in which either the first diene monomer or the second diene monomer has an internal double bond comprising a disubstituted vinyl group or a tri-substituted vinyl group having one or more methyl group substituents.
- 8. The process of claim 1, on which the first diene monomer is an α, internal non-conjugated diene monomer having an internal double bond comprising a tri-substituted vinyl group having two methyl group substituents.
- 9. The process of claim 1, in which the second diene monomer is an α, ω diene comprising unsubstituted 1,4-pentadiene; 1,5-hexadiene; 1,6-heptadiene; 1,7-octadiene; 1,8-nonadiene; or 1,9-decadiene.
- 10. The process of claim 1, in which either the first diene monomer or the second diene monomer comprising substituted 1,4-pentadiene; 1,5-hexadiene; 1,6-heptadiene; 1,7-octadiene; 1,8-nonadiene; or 1,9-decadiene.
- 11. The process of claim 1, in which the second diene monomer comprises 2-methyl-1,5-hexadiene.
- 12. The process of claim 1, in which the first diene monomer comprises 2-methyl-1,5-hexadiene or 7-methyl-1,6-octadiene.
- 13. The process of claim 1, in which the amount of the first diene monomer is greater than the amount of the second diene monomer.
- 14. The process of claim 1, in which the first diene monomer is an α, internal non-conjugated diene monomer; the second diene monomer is an α, ω non-conjugated diene monomer; and the amount of the first diene monomer is greater than the amount of the second diene monomer.
- 15. The process of claim 1, in which the polymerization medium includes 50 mol % or more propylene monomers, 10 mol % or less α, internal non-conjugated diene monomers, and 1 mol % or less α, ω non-conjugated diene monomers.
- 16. The process of claim 1, in which the metallocene catalyst compound is or includes a substituted or unsubstituted silyl-bridged or ethylene-bridged bis-indenyl metallocene.
- 17. The process of claim 1, in which the metallocene compound comprises a bridged metallocene compound having at least two indenyl rings or derivatives of indenyl rings, each ring being substituted at the 2 position.
- 18. The process of claim 1, in which the metallocene compound comprises a bridged metallocene compound having at least two indenyl rings or derivatives of indenyl rings, each ring being substituted at the 2 and 4 positions.
- 19. The process of claim 1, in which the metallocene compound comprises supported dimethylsilylbis(2-methyl-4-phenyl-1-indenyl)zirconium dimethyl.
- 20. The process of claim 1, in which the metallocene includes a dimethylanilinium tetrakis (perfluorophyl)boron activator.
- 21. The process of claim 1, in which the supported metallocene includes a methlyaluminoxane activator.
- 22. The process of claim 1, in which the metallocene compound is represented by the formula:
- 23. The process of claim 1, in which the metallocene compound is represented by the formula:
- 24. The process of claim 1, in which the polymerization medium is substantially gel-free following formation of the polypropylene terpolymer.
- 25. The process of claim 1, further comprising crosslinking the polypropylene terpolymer.
- 26. The process of claim 1, in which polymerization medium has less than 90 volume percent diluent.
- 27. The process of claim 1, in which polymerization medium has less then 50 volume percent diluent.
- 28. The process of claim 1, in which polymerization medium has less then 30 volume percent diluent.
- 29. The process of claim 1, in which the final crystalline polypropylene terpolymer is isotactic or syndiotactic.
- 30. The process of claim 1, in which the metallocene catalyst compound is combined with the monomers in the absence of hydrogen or in the presence of hydrogen in an amount of up to 1.0 mole % hydrogen in the reactor.
- 31. The process of claim 1, in which the heat of fusion of the crystalline polypropylene is 50 J/g or more.
- 32. The process of claim 1, in which the heat of fusion of the branched crystalline polypropylene is 70 J/g or more. Add 75 j/g more
- 33. The process of claim 1, in which the heat of fusion of the branched crystalline polypropylene is 100 J/g or more.
- 34. The process of claim 1, in which the branched crystalline polypropylene has a Branching Index of 0.98 or less.
- 35. The process of claim 1, in which the branched crystalline polypropylene has a Branching Index of 0.95 or less.
- 36. The process of claim 1, in which the branched crystalline polypropylene has a Branching Index of 0.90 or less.
- 37. The process of claim 1, in which the branched crystalline polypropylene has a Branching Index of 0.80 or less.
- 38. A polymer composition that includes a branched crystalline diene-modified polypropylene random terpolymer having propylene units; first diene units; second diene units; from 0.0 wt % to 2.0 wt % ethylene units; and a heat of fusion of 30 J/g or more, wherein the first diene units and the second diene units are derived from different non-conjugated diene monomers, each having 5 or more carbon atoms.
- 39. The polymer composition of claim 38, in which the random polypropylene terpolymer comprises at least 30% and no more than 95% propylene units; at least 5% and no more than 65% first diene units; at least 0.001% and no more than 2.00% second diene units; and from 0.0 mol % to 3.0 mol % ethylene units.
- 40. The polymer composition of claim 38, in which the first diene units are derived from α, internal non-conjugated diene monomers.
- 41. The polymer composition of claim 38, in which the second diene units are derived from α, ω non-conjugated diene monomers.
- 42. The polymer composition of claim 38, in which the first diene monomer is an α, internal non-conjugated diene monomer that is present in the polypropylene terpolymer in an amount of from 0.0005 mol % to 10 mol %.
- 43. The polymer composition of claim 38, in which the first diene monomer is an α, internal non-conjugated diene monomer that is present in the polypropylene terpolymer in an amount of from 0.005 mol % to 1 mol %.
- 44. The polymer composition of claim 38, in which the first diene monomer is an α, internal non-conjugated diene monomer selected from the group consisting of 2-methyl-1,5-hexadiene and 7-methyl-1,6-octadiene.
- 45. The polymer composition of claim 38, in which the branched final crystalline polypropylene has a crystallization temperature (Tc) of 50° C. or more.
- 46. The polymer composition of claim 38, in which the branched crystalline polypropylene has a crystallization temperature (Tc) of 75° C. or more.
- 47. The polymer composition of claim 38, in which the branched crystalline polypropylene has a crystallization temperature (Tc) of 100° C. or more.
- 48. The polymer composition of claim 38, in which the branched crystalline polypropylene has a crystallization temperature (Tc) of 110° C. or more.
- 49. The polymer composition of claim 38, in which the branched crystalline polypropylene has a crystallization temperature (Tc) of from 50° C. to 115° C.
- 50. The polymer composition of claim 38, in which the branched crystalline polypropylene has a melting point (Tm) of 75° C. or more.
- 51. The polymer composition of claim 38, in which the branched crystalline polypropylene has a melting point (Tm) of 100° C. or more.
- 52. The polymer composition of claim 38, in which the branched crystalline polypropylene has a melting point (Tm) of 125° C. or more.
- 53. The polymer composition of claim 38, in which the branched crystalline polypropylene has a melting point (Tm) of 150° C. or more.
- 54. The polymer composition of claim 38, in which the branched crystalline polypropylene has a melting point (Tm) of 160° C. or more.
- 55. The polymer composition of claim 38, in which the branched crystalline polypropylene has a melting point (Tm) of from 75° C. to 160° C.
- 56. The polymer composition of claim 38, in which the branched crystalline polypropylene has a melt flow rate of 0.01 or more.
- 57. The polymer composition of claim 38, in which the branched crystalline polypropylene has a melt flow rate of 0.1 or more.
- 58. The polymer composition of claim 38, in which the branched crystalline polypropylene has a melt flow rate of 0.5 or more.
- 59. The polymer composition of claim 38, in which the branched crystalline polypropylene has a melt flow rate of 0.7 or more.
- 60. The polymer composition of claim 38, in which the branched crystalline polypropylene has a melt flow rate of 1.0 or more.
- 61. The polymer composition of claim 38, in which the branched crystalline polypropylene has a melt flow rate of 1.5 or more.
CROSS REFERENCE TO RELATED APPLICATIONS
[0001] This application claims the benefit of Provisional Application No. 60/442,718 filed Jan. 27, 2003 and 60/431,088, filed Dec. 5, 2002.
Provisional Applications (2)
|
Number |
Date |
Country |
|
60442718 |
Jan 2003 |
US |
|
60431088 |
Dec 2002 |
US |