Abstract:
A film formed from a polyethylene copolymer using a reduced chromium oxide catalyst, ethylene monomers and a co-monomer selected from butene monomers or 1-hexene, where the polyethylene copolymer has a density in the range of from about 0.935 to about 0.950 g/cm 3 and an I 21 /I 5 in a range of about 18.0 to about 30.0. The film formed from the polyethylene copolymer has a dart drop impact (g/μm) that significantly greater as compared to a film of the polyethylene copolymer formed using a silyl chromate catalyst in place of the reduced chromium oxide catalyst. A method of making such films is also provided.
Abstract translation:使用还原的氧化铬催化剂,乙烯单体和选自丁烯单体或1-己烯的共聚单体由聚乙烯共聚物形成的膜,其中聚乙烯共聚物的密度范围为 约0.935至约0.950g / cm 3和约21.0至约30.0的I 21 / I 5。 与使用甲硅烷基铬酸盐催化剂代替还原的氧化铬催化剂形成的聚乙烯共聚物膜相比,由聚乙烯共聚物形成的膜具有明显更大的落镖冲击(g /μm)。 还提供了制作这种胶片的方法。 p>
Abstract:
Polymers, and systems and methods for making and using the same are described herein. A polymer includes ethylene and at least one alpha olefin having from 4 to 20 carbon atoms. The polymer is formed by a trimmed catalyst system including a supported catalyst including bis(n-propylcyclopentadienyl) hafnium (R 1 )(R 2 ) and a trim catalyst comprising meso-O(SiMe 2 lnd) 2 Zr 2 (R 1 )(R 2 ), wherein R 1 and R 2 are each, independently, methyl, chloro, fluoro, or a hydrocarbyl group.
Abstract:
A polymerization catalyst system and polymerization processes using the catalyst systems are disclosed. The polymerization catalyst systems may include a) a first catalyst compound, and b) a second catalyst compound, wherein the first catalyst compound includes an oxadiazole-containing compound. In some embodiments, the oxadiazole-containing compound has essentially no hydrogen response, thus allowing better and / or tailored control of product properties when producing polymers using the catalyst system.
Abstract:
Polymers, and systems and methods for making and using the same are described herein. A polymer includes ethylene and at least one alpha olefin having from 4 to 20 carbon atoms. The polymer has a melt index ratio (MIR) greater than about 40. The polymer also has a value for Mw1/Mw2 of at least about 2.0, wherein Mw1/Mw2 is a ratio of a weight average molecular weight (Mw) for a first half of a temperature rising elution (TREF) curve from a cross-fractionation (CFC) analysis to an Mw for a second half of the TREF curve. The polymer also has a value for Tw1 - Tw2 of less than about -15 °C, wherein Tw1 - Tw2 is a difference of a weight average elution temperature (Tw) for the first half of the TREF curve to a Tw for the second half of the TREF curve.
Abstract:
Olefin polymerization catalyst systems including a high molecular weight catalyst compound and a low molecular weight catalyst compound, and methods of making same are provided. High molecular weight catalysts include metallocene catalysts and low molecular weight catalysts include non-metallocene compounds including biphenyl phenol compounds. Generally catalyst systems may include less than about 5.0 mol% of the high molecular weight catalyst compound relative to said low molecular weight catalyst. Methods for olefin polymerization including the aforementioned catalyst systems, and polyolefins and products made therefrom.
Abstract:
An ethylene polymer including units derived from ethylene, at least one other alpha-olefin comonomer, and at least one diene, and having at least one of certain properties disclosed herein.
Abstract:
A process for polymerizing olefin(s) utilizing a cyclic bridged metallocene catalyst system to produce polymers with improved properties is provided. The catalyst system may include a cyclic bridged metallocene, LA(R'SiR')L B ZrQ 2 , activated by an activator, the activator comprising aluminoxane, a modified aluminoxane, or a mixture thereof, and supported by a support, where: L A and L B are independently an unsubstituted or a substituted cyclopentadienyl ligand bonded to Zr and defined by the formula (C 5 H 4 - d R d ), where R is hydrogen, a hydrocarbyl substituent, a substituted hydrocarbyl substituent, or a heteroatom substituent, and where d is O, 1, 2, 3 or 4; L A and L B are connected to one another with a cyclic silicon bridge, R' SiR', where R' are independently hydrocarbyl or substituted hydrocarbyl substituents that are connected with each other to form a silacycle ring; and each Q is a labile hydrocarbyl or a substituted hydrocarbyl ligand.
Abstract:
A catalyst composition that includes a support material having an improved particle-size distribution is provided. Processes for producing polyolefin composition also are provided. Polymers and films also are provided. An example of a catalyst composition is a supported multi-transition-metal catalyst composition that includes: (a) at least two catalyst components selected from the group consisting of: a nonmetallocene catalyst component and a metallocene catalyst component; (b) a support material that has a D 50 of less than about 30 microns and a particle size distribution having a D 90 /D 10 ratio of less than about 6; and (c) an activator.
Abstract translation:提供了包括具有改善的粒度分布的载体材料的催化剂组合物。 还提供了生产聚烯烃组合物的方法。 还提供聚合物和薄膜。 催化剂组合物的实例是负载型多过渡金属催化剂组合物,其包括:(a)至少两种选自非茂金属催化剂组分和茂金属催化剂组分的催化剂组分; (b)具有小于约30微米的D≤50的支撑材料和具有D 90 N / D 10 N的粒度分布, 比例小于6; 和(c)活化剂。
Abstract:
Methods of tailoring polyethylenes are contemplated utilizing 0.5 to 7.95 volume percent oxygen containing gases. The tailoring occurs in a melt-conveying zone of a mixer/extruder, and not in the feed or melting zones of a mixer/extruder. The effect of tailoring is to increase elasticity (G'/G") of the polyethylenes more than 10 percent over similar polyethylenes that are extruded/mixed in the substantial absence of oxygen or oxygen containing gases.
Abstract:
Methods of tailoring polyethylenes are contemplated utilizing 0.5 to 70 volume percent oxygen containing gases. The tailoring occurs in a melt-conveying zone of a mixer/extruder, and not in the feed or melting zones of a mixer/extruder. The effect of tailoring is to decrease the haze and/or increase the gloss of blown films made from the tailored polyethylenes compared to similar polyethylenes that are extruded/mixed in the substantial absence of oxygen or oxygen containing gases.