초록

Methods for controlling properties of an olefin polymer using an alcohol compound are disclosed. The MI and the HLMI of the polymer can be decreased, and the Mw and the Mz of the polymer can be increased, via the addition of the alcohol compound.

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1. A method of controlling a polymerization reaction in a polymerization reactor system, the method comprising: (i) contacting a dual catalyst system with ethylene and a C3-C10 alpha-olefin comonomer in the polymerization reactor system under polymerization conditions to produce an ethylene copolyme

1. A method of controlling a polymerization reaction in a polymerization reactor system, the method comprising: (i) contacting a dual catalyst system with ethylene and a C3-C10 alpha-olefin comonomer in the polymerization reactor system under polymerization conditions to produce an ethylene copolymer,wherein the dual catalyst system comprises a first metallocene catalyst component, a second metallocene catalyst component, an activator, and a co-catalyst;wherein the polymerization reactor system comprises a slurry reactor, a gas-phase reactor, a solution reactor, or a combination thereof; and(ii) introducing an amount of an alcohol compound into the polymerization reactor system to (I) reduce a melt index parameter of the ethylene copolymer; (II) increase a molecular weight parameter of the ethylene copolymer selected from Mw, Mz, or both; or (III) reduce a melt index parameter of the ethylene copolymer and increase a molecular weight parameter of the ethylene copolymer selected from Mw, Mz, or both. 2. The method of claim 1, wherein the alcohol compound comprises a C1 to C12 mono alcohol. 3. The method of claim 1, wherein the alcohol compound comprises ethylene glycol, propylene glycol, or both. 4. The method of claim 1, wherein the polymerization reactor system comprises two or more reactors. 5. The method of claim 1, wherein the activator comprises an aluminoxane compound, an organoboron or organoborate compound, an ionizing ionic compound, or any combination thereof. 6. The method of claim 1, wherein: the polymerization reactor system comprises a loop slurry reactor;the alcohol compound comprises methanol, ethanol, propanol, butanol, pentanol, hexanol, or a combination thereof;the ethylene copolymer is an ethylene/1-butene copolymer, an ethylene/1-hexene copolymer, or an ethylene/1-octene copolymer; anda weight ratio of the first metallocene catalyst component to the second metallocene catalyst component is in a range of from about 1:15 to about 15:1. 7. The method of claim 1, wherein: the activator comprises an activator-support comprising a fluorided solid oxide, a sulfated solid oxide, or a combination thereof; andthe co-catalyst comprises an organoaluminum compound. 8. The method of claim 7, wherein the amount of the alcohol compound introduced into the polymerization reactor system is in a range from about 1:2500 to about 1:250, based on the moles of hydroxyl (—OH) groups of the alcohol compound to the weight of the activator-support in grams added to the polymerization reactor system. 9. The method of claim 7, wherein the amount of the alcohol compound introduced into the polymerization reactor system is in a molar ratio range of from about 0.15:1 to about 0.85:1, based on the moles of hydroxyl (—OH) groups of the alcohol compound to the moles of the organoaluminum compound added to the polymerization reactor system. 10. The method of claim 7, wherein: the first metallocene catalyst component comprises an unbridged metallocene compound containing zirconium; andthe second metallocene catalyst component comprises a bridged metallocene compound containing zirconium or hafnium. 11. The method of claim 10, wherein the amount of the alcohol compound introduced into the polymerization reactor system is in a molar ratio range of from about 20:1 to about 500:1, based on the ratio of the moles of hydroxyl (—OH) groups of the alcohol compound to the total moles of the first metallocene catalyst component and the second metallocene catalyst component added to the polymerization reactor system. 12. The method of claim 11, wherein: the first metallocene catalyst component comprises an unbridged zirconium based metallocene compound containing two cyclopentadienyl groups, two indenyl groups, or a cyclopentadienyl and an indenyl group; andthe second metallocene catalyst component comprises a bridged zirconium or hafnium based metallocene compound with a cyclopentadienyl group and fluorenyl group. 13. A process for producing an olefin polymer with a target melt index parameter, a target molecular weight parameter, or a target melt index parameter and a target molecular weight parameter, the process comprising: (a) contacting a dual catalyst system with an olefin monomer and an optional olefin comonomer in a polymerization reactor system under polymerization conditions,wherein the dual catalyst system comprises a first metallocene catalyst component, a second metallocene catalyst component, an activator, and a co-catalyst;wherein the olefin monomer comprises ethylene or propylene; and(b) controlling an amount of an alcohol compound introduced into the polymerization reactor system to produce the olefin polymer with the target melt index parameter, the target molecular weight parameter, or the target melt index parameter and the target molecular weight parameter; wherein:the melt index parameter is MI, HLMI, or both; andthe molecular weight parameter is Mw, Mz, or both. 14. The process of claim 13, wherein the MI and HLMI of the olefin polymer decrease as the amount of the alcohol compound added to the polymerization reactor system increases. 15. The process of claim 14, wherein: the polymerization reactor system comprises a slurry reactor, a gas-phase reactor, a solution reactor, or a combination thereof;the alcohol compound comprises methanol, ethanol, propanol, butanol, pentanol, hexanol, or a combination thereof; andthe olefin monomer comprises propylene. 16. The process of claim 14, wherein: the first metallocene catalyst component comprises an unbridged metallocene compound containing zirconium;the second metallocene catalyst component comprises a bridged metallocene compound containing zirconium or hafnium;the activator comprises an activator-support comprising a fluorided solid oxide, a sulfated solid oxide, or a combination thereof; andthe co-catalyst comprises an organoaluminum compound. 17. The process of claim 16, wherein: the polymerization reactor system comprises a loop slurry reactor;the alcohol compound comprises isopropyl alcohol;the first metallocene catalyst component comprises an unbridged zirconium based metallocene compound containing two cyclopentadienyl groups, two indenyl groups, or a cyclopentadienyl and an indenyl group;the second metallocene catalyst component comprises a bridged zirconium or hafnium based metallocene compound with a cyclopentadienyl group and fluorenyl group; andthe olefin polymer is an ethylene homopolymer or an ethylene/α-olefin copolymer characterized by a MI of less than about 10 g/10 min, and a Mw/Mn ratio in a range from about 10 to about 40. 18. The process of claim 13, wherein the Mw and Mz of the olefin polymer increase as the amount of the alcohol compound added to the polymerization reactor system increases. 19. The process of claim 18, wherein: the activator comprises an activator-support comprising fluorided alumina, sulfated alumina, fluorided silica-alumina, sulfated silica-alumina, fluorided silica-zirconia, fluorided silica-coated alumina, sulfated silica-coated alumina, or any combination thereof; andthe co-catalyst comprises an organoaluminum compound comprising trimethylaluminum, triethylaluminum, tri-n-propylaluminum, tri-n-butylaluminum, triisobutylaluminum, tri-n-hexylaluminum, tri-n-octylaluminum, diisobutylaluminum hydride, diethylaluminum ethoxide, diethylaluminum chloride, or any combination thereof. 20. The process of claim 19, wherein: the first metallocene catalyst component comprises an unbridged metallocene compound containing zirconium; andthe second metallocene catalyst component comprises a bridged metallocene compound containing zirconium or hafnium. 21. The process of claim 13, wherein: the olefin polymer comprises a higher molecular weight component and a lower molecular weight component; anda weight ratio of the higher molecular weight component to the lower molecular weight component increases as the amount of the alcohol compound added to the polymerization reactor system increases. 22. The process of claim 21, wherein: the polymerization reactor system comprises a slurry reactor, a gas-phase reactor, a solution reactor, or a combination thereof;the alcohol compound comprises methanol, ethanol, propanol, butanol, pentanol, hexanol, or a combination thereof;the olefin polymer is an ethylene homopolymer, an ethylene/1-butene copolymer, an ethylene/1-hexene copolymer, or an ethylene/1-octene copolymer; andthe weight ratio of the higher molecular weight component to the lower molecular weight component is in a range from about 1:15 to about 15:1. 23. The process of claim 22, further comprising a step of adding hydrogen to the polymerization reactor system, or a step of adjusting a weight ratio of the first metallocene catalyst component to the second metallocene catalyst component, or both.