초록 ▼

This invention relates to a process for polymerizing olefins in which the amount of trimethylaluminum in a methylalumoxane solution is adjusted to be from 6 to 25 mole %, prior to use as an activator, where the mole % trimethylaluminum is determined by 1H NMR of the solution prior to combination wit

This invention relates to a process for polymerizing olefins in which the amount of trimethylaluminum in a methylalumoxane solution is adjusted to be from 6 to 25 mole %, prior to use as an activator, where the mole % trimethylaluminum is determined by 1H NMR of the solution prior to combination with any support. This invention also relates to a process for polymerizing olefins in which the amount of an unknown species present in a methylalumoxane solution is adjusted to be from 0.10 to 0.65 integration units prior to use as an activator, where the unknown species is the peak is identified in the 1H NMR spectra of the solution performed prior to combination with any support. Preferably, the methylalumoxane solution is present in a catalyst system also comprising a metallocene transition metal compound.

대표청구항 ▼

1. A process for adjusting the properties of a linear low density polyethylene while polymerizing ethylene and hexene to produce a linear low density polyethylene in which the amount of trimethylaluminum in a methylalumoxane solution is reduced within the range from 25 mole % to 1 mole % at a given

1. A process for adjusting the properties of a linear low density polyethylene while polymerizing ethylene and hexene to produce a linear low density polyethylene in which the amount of trimethylaluminum in a methylalumoxane solution is reduced within the range from 25 mole % to 1 mole % at a given hydrogen concentration in order to decrease the weight percent of medium density polyethylene component produced, prior to use as an activator, where the mole % trimethylaluminum is determined by 1H NMR, on the basis of the aluminum content, of the solution prior to combination with any support and wherein: 1) the methylalumoxane solution is present in a catalyst system also comprising a hafnium metallocene transition metal compound;2) the catalyst system, prior to combination with any support, has an aluminum to transition metal molar ratio of 175:1 or less;3) the olefins comprise ethylene; and4) a polymer comprising at least 50 mol % ethylene units is obtained. 2. The process of claim 1, wherein the amount of trimethylaluminum is adjusted by removing trimethylaluminum. 3. The process of claim 1, wherein the catalyst system in methylalumoxane solution prior to combination with any support has an aluminum to transition metal molar ratio of 175:1 to 50:1. 4. The process of claim 1, wherein the metallocene transition metal compound is represented by the formula: CpACpBHfX*n wherein each X* and each Cp group is chemically bonded to Hf, n is 1 or 2, CpA and CpB may be the same or different cyclopentadienyl ligands or ligands isolobal to cyclopentadienyl, either or both of which may contain heteroatoms and either or both of which may be substituted. 5. The process of claim 4, wherein CpA and CpB are independently selected from the group consisting of cyclopentadienyl, indenyl, tetrahydroindenyl, fluorenyl, and substituted derivatives of each. 6. The process of claim 1, wherein the metallocene transition metal compound comprises a bis(n-C3-4 alkyl cyclopentadienyl) hafnium dialkyl or dihalide. 7. The process of claim 1, wherein the metallocene transition metal compound comprises bis(n-propyl cyclopentadienyl) hafnium dichloride and/or bis(n-propyl cyclopentadienyl) hafnium dimethyl. 8. The process of claim 1, wherein the catalyst system is contacted with one or more olefins. 9. The process of claim 8, wherein the polymerization process is a gas phase process. 10. The process of claim 9, wherein the olefins comprise ethylene and the ethylene partial pressure in the gas phase polymerization is from 50 to 250 psi (345 to 1724 kPa). 11. The process of claim 8, wherein the polymerization process is a slurry phase process. 12. The process of claim 8, wherein the olefins comprise ethylene and at least one C3 to C20 olefin. 13. The process of claim 12, wherein the C3 to C20 olefin is one or more of propylene, butene, hexene, and octene. 14. The process of claim 12, wherein the C3 to C20 olefin is hexene. 15. The process of claim 1, wherein the amount of trimethylaluminum is adjusted by adding trimethylaluminum to the methylalumoxane solution. 16. A process for polymerizing olefins to produce a linear low density polyethylene having a density of from 0.916 to 0.917 g/cm3 in which the amount of trimethylaluminum in a methylalumoxane solution is reduced within the range from 25 mole % to 1 mole % at a given hydrogen concentration in order to decrease the weight percent of medium density polyethylene component produced, prior to use as an activator, where the mole % trimethylaluminum is determined by 1H NMR, on the basis of the aluminum content, of the solution prior to combination with any support and in which the amount of an unknown species present in a methylalumoxane solution is adjusted to be from 0.10 to 0.65 integration units, prior to use as an activator, wherein the integration units are defined on the basis of the TMA peak being normalized to 3.0, and where the unknown species is identified in the 1H NMR spectra of the solution prior to combination with any support, wherein the methylalumoxane solution is present in a catalyst system also comprising a hafnium metallocene transition metal compound and the catalyst system, prior to combination with any support, has an aluminum to transition metal molar ratio of 175:1 to 50:1 wherein the hafnium metallocene transition metal compound is represented by the formula: CpACpBHfX*n wherein each X* and each Cp group is chemically bonded to Hf, n is 1 or 2, CpA and CpB are independently selected from the group consisting of cyclopentadienyl, indenyl, tetrahydroindenyl, fluorenyl, and substituted derivatives of each. 17. The process of claim 16, wherein the metallocene transition metal compound comprises a bis(n-C3-4 alkyl cyclopentadienyl) hafnium dialkyl or dihalide. 18. The process of claim 16, wherein the metallocene transition metal compound comprises bis(n-propyl cyclopentadienyl) hafnium dichloride and/or bis(n-propyl cyclopentadienyl) hafnium dimethyl. 19. The process of claim 16, wherein the catalyst system is contacted with ethylene and at least one of propylene, butene, hexene, and octene. 20. The process of claim 16, wherein the polymerization process is a gas phase process and the ethylene partial pressure in the gas phase polymerization is from 50 to 250 psi (345 to 1724 kPa) or a slurry phase process. 21. The process of claim 1, wherein the polyolefin comprises ethylene and from 0.5 to 25 mole % of C3 to C20 olefin comonomer, said copolymer having: 1) a ratio of Ultimate Tensile Stress to Tensile Stress at 100% elongation of 2.5 or more; 2) a ratio of Ultimate Tensile Stress to Tensile Stress at 300% elongation of 2.4 or more; 3) a ratio of Ultimate Tensile Stress to Tensile Stress at the primary yield point of 2.9 or more; 4) a density of 0.910 g/cm3 or more; 5) a 1% secant modulus of 30 to 100 MPa; 6) a Tensile Stress of Y MPa or more, where Y=(0.0532)*Z−8.6733 and Z is the percent strain and is a number from 500 to 2000; and 7) a 1% secant modulus of 40 to 100 MPa.