초록

Methods for controlling properties of an olefin polymer using an organozinc compound are disclosed. The HLMI/MI shear ratio of the polymer can be decreased and the Mz/Mw ratio of the polymer can be increased via the addition of the organozinc 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 an olefin monomer and an optional olefin comonomer in the polymerization reactor system under polymerization conditions to produce an olefin poly

1. A method of controlling a polymerization reaction in a polymerization reactor system, the method comprising: (i) contacting a dual catalyst system with an olefin monomer and an optional olefin comonomer in the polymerization reactor system under polymerization conditions to produce an olefin polymer,wherein the dual catalyst system comprises a first metallocene catalyst component and a second metallocene catalyst component; and(ii) introducing an amount of an organozinc compound into the polymerization reactor system to reduce a HLMI/MI shear ratio and/or to increase a Mz/Mw ratio of the olefin polymer. 2. The method of claim 1, wherein the organozinc compound comprises a compound having the formula: Zn(X10)(X11); wherein:X10 is a C1 to C18 hydrocarbyl group; andX11 is H, a halide, a C1 to C18 hydrocarbyl group, or a C1 to C18 hydrocarboxy group. 3. The method of claim 1, wherein the dual catalyst system comprises: a first metallocene catalyst component comprising an unbridged metallocene compound containing zirconium or an unbridged dinuclear metallocene compound containing zirconium;a second metallocene catalyst component comprising a bridged metallocene compound containing zirconium or hafnium; andan activator comprising an activator-support, an aluminoxane compound, an organoboron or organoborate compound, an ionizing ionic compound, or any combination thereof. 4. The method of claim 3, wherein: the activator comprises an activator-support comprising fluorided alumina, chlorided alumina, bromided alumina, sulfated alumina, fluorided silica-alumina, chlorided silica-alumina, bromided silica-alumina, sulfated silica-alumina, fluorided silica-zirconia, chlorided silica-zirconia, bromided silica-zirconia, sulfated silica-zirconia, fluorided silica-titania, fluorided silica-coated alumina, sulfated silica-coated alumina, phosphated silica-coated alumina, or any combination thereof; andthe amount of the organozinc compound introduced into the polymerization reactor system is in a range from about 2 to about 100 wt. %, based on the weight of the activator-support added to the polymerization reactor system. 5. The method of claim 1, wherein the polymerization reactor system comprises a slurry reactor, a gas-phase reactor, a solution reactor, or a combination thereof. 6. The method of claim 1, wherein the polymerization reactor system comprises a single reactor. 7. The method of claim 1, wherein the olefin monomer comprises ethylene and the olefin comonomer comprises a C3-C10 alpha-olefin. 8. The method of claim 1, further comprising: determining the HLMI/MI shear ratio, and adjusting the amount of the organozinc compound introduced into the polymerization reactor system based on the difference between the determined HLMI/MI shear ratio and a target HLMI/MI shear ratio; ordetermining the Mz/Mw ratio, and adjusting the amount of the organozinc compound introduced into the polymerization reactor system based on the difference between the determined Mz/Mw ratio and a target Mz/Mw ratio; orboth. 9. The method of claim 1, wherein a weight ratio of the first metallocene catalyst component to the second metallocene catalyst component is in a range of from about 1:10 to about 10:1. 10. The method of claim 1, wherein a weight ratio of the first metallocene catalyst component to the second metallocene catalyst component is substantially constant. 11. The method of claim 1, wherein the amount of the organozinc compound introduced into the polymerization reactor system is in a molar ratio range of from about 5:1 to about 200:1, based on the ratio of the moles of the organozinc 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 1, further comprising: a step of adjusting a weight ratio of the first metallocene catalyst component to the second metallocene catalyst component; ora step of adding hydrogen to the polymerization reactor system to adjust a molecular weight parameter and/or a melt index of the olefin polymer; orboth. 13. A process for producing an olefin polymer with a target HLMI/MI shear ratio and/or a target Mz/Mw ratio, 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 and a second metallocene catalyst component; and(b) controlling an amount of an organozinc compound introduced into the polymerization reactor system to produce the olefin polymer with the target HLMI/MI shear ratio and/or the target Mz/Mw ratio. 14. The process of claim 13, wherein the olefin polymer has: a melt index (MI) of less than about 10 g/10 min;a number-average molecular weight (Mn) in a range from about 5,000 to about 40,000 g/mol;a weight-average molecular weight (Mw) in a range from about 100,000 to about 350,000 g/mol; ora Mw/Mn ratio in a range from about 5 to about 40; orany combination thereof. 15. The process of claim 14, wherein the organozinc compound comprises diethylzinc, and the olefin polymer is an ethylene/α-olefin copolymer. 16. The process of claim 13, wherein the HLMI/MI shear ratio of the olefin polymer decreases as the amount of the organozinc compound added to the polymerization reactor system increases. 17. The process of claim 13, wherein the Mz/Mw ratio of the olefin polymer increases as the amount of the organozinc compound added to the polymerization reactor system increases. 18. The process of claim 13, wherein the olefin polymer comprises a higher molecular weight component and a lower molecular weight component, and wherein: a weight ratio of the higher molecular weight component to the lower molecular weight component decreases as the amount of the organozinc compound added to the polymerization reactor system increases;a peak molecular weight of the lower molecular weight component increases as the amount of the organozinc compound added to the polymerization reactor system increases; ora peak molecular weight of the higher molecular weight component is substantially unchanged as the amount of the organozinc compound added to the polymerization reactor system increases; orany combination thereof. 19. The process of claim 13, wherein: the polymerization reactor system comprises a loop slurry reactor;the organozinc compound comprises diethylzinc; andthe olefin polymer is an ethylene/1-hexene copolymer. 20. The process of claim 19, wherein the dual catalyst system comprises: a first metallocene catalyst component comprising an unbridged metallocene compound containing zirconium or an unbridged dinuclear metallocene compound containing zirconium;a second metallocene catalyst component comprising a bridged metallocene compound containing zirconium or hafnium;an activator-support comprising a solid oxide treated with an electron-withdrawing anion; andan organoaluminum compound.