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    • 34. 发明授权
    • Catalyst system for the preparation of a rubbery copolymer
    • 用于制备橡胶状共聚物的催化剂体系
    • US6150483A
    • 2000-11-21
    • US25339
    • 1998-02-18
    • Jacob RenkemaPeter J. H. Windmuller
    • Jacob RenkemaPeter J. H. Windmuller
    • C08F4/685C08F10/00C08F110/02C08F210/16C08F4/52
    • C08F10/00C08F210/16C08F110/02
    • The invention relates to a catalyst system and a process suited for the preparation of a rubbery copolymer of ethylene, one or more .alpha.-olefins and optionally one or more polyunsaturated compounds, in which the catalyst system comprises a vanadium compound, an organometal compound and optionally a promoter, characterized in that the organometal complex in the catalyst system is an imido complex that satisfies the general formula(R.sub.u -X.sup.1.sub.v -Me.sup.1).sub.n =NR.sup.1 (I)where each individual Me.sup.1 is a metal chosen from group 1, 2, 12 or 13 of the Periodic System of Elements, each individual R is hydrogen or a hydrocarbon group having 1-20 C atoms, N--R.sup.1 is an imido group where R.sup.1 is hydrogen or a hydrocarbon group having 1-20 C atoms or a group with the general formula MR.sup.3.sub.3, where M is an element chosen from group 14 of the Periodic System of Elements, each individual R.sup.3 is hydrogen, a hydrocarbon group having 1-20 C atoms or a heteroatom-containing group, X.sup.1 is a halogen atom and n.gtoreq.1; u>0, v.gtoreq.0; u+v+2/n=p, where p=valency of Me.sup.1.
    • 本发明涉及一种催化剂体系和适用于制备乙烯,一种或多种α-烯烃和任选的一种或多种多不饱和化合物的橡胶状共聚物的方法,其中催化剂体系包含钒化合物,有机金属化合物和任选的 其特征在于,催化剂体系中的有机金属络合物是满足通式(Ru-X1v-Me1)n = NR1(I)的亚氨基络合物,其中各个Me1为选自第1,2,12族的金属 或元素周期表中的13个,每个单独的R是氢或具有1-20个C原子的烃基,N-R 1是其中R 1是氢或具有1-20个C原子的烃基或与 通式MR33,其中M是选自元素周期元素系14的元素,各个基团R 3为氢,具有1-20个C原子的烃基或含杂原子的基团,X 1为卤素原子,n为 > / = 1; u> 0,v> / = 0; u + v + 2 / n = p,其中p = Me1的化合价。
    • 36. 发明授权
    • Olefin polymerization method
    • 烯烃聚合法
    • US5369194A
    • 1994-11-29
    • US23135
    • 1993-02-24
    • Leonard V. CribbsMichael W. Lynch
    • Leonard V. CribbsMichael W. Lynch
    • C08F2/06C08F4/60C08F4/633C08F4/64C08F4/659C08F4/685C08F10/00C08F10/02C08F4/68
    • C08F10/02
    • A multiple site solid catalyst component capable of producing polyolefins having a broad or multimodal molecular weight distribution, such as a bimodal molecular weight distribution, is prepared by contacting a particulate solid support with a zirconium compound or complex to bind the zirconium compound or complex to the support, optionally followed by contacting the supported zirconium compound or complex with a Lewis acid to produce an intermediate product, optionally isolating and washing the supported zirconium compound or complex or resulting intermediate product to remove soluble by-products therefrom, and reacting the washed or unwashed supported zirconium compound or complex or intermediate product with a titanium or vanadium compound to produce a solid catalyst component.
    • 通过使颗粒状固体载体与锆化合物或络合物接触,将锆化合物或络合物与锆的化合物或络合物接触,制备能够生产具有宽或多峰分子量分布如双峰分子量分布的聚烯烃的多部位固体催化剂组分 任选地将负载的锆化合物或络合物与路易斯酸接触以产生中间产物,任选地分离和洗涤负载的锆化合物或络合物或所得中间产物以从其中除去可溶性副产物,并将洗涤或未洗涤的 负载的锆化合物或复合物或中间产物与钛或钒化合物反应以产生固体催化剂组分。
    • 37. 发明授权
    • Silica supported transition metal catalyst
    • 二氧化硅负载过渡金属催化剂
    • US5231151A
    • 1993-07-27
    • US854175
    • 1992-03-20
    • Lee SpencerBrian W. S. KolthammerMiriam P. RipplingerJeffrey J. WoosterPak-Wing S. ChumJacquelyn A. deGroot
    • Lee SpencerBrian W. S. KolthammerMiriam P. RipplingerJeffrey J. WoosterPak-Wing S. ChumJacquelyn A. deGroot
    • C08J5/18B29C55/02B29K23/00B29L7/00C08F4/646C08F4/658C08F4/685C08F10/00C08F210/00C08F210/02C08F210/16
    • C08F10/00Y10S428/91Y10T428/26Y10T428/31855
    • A transition metal containing catalyst useful for the polymerization of .alpha.-olefins is prepared by (A) forming in an inert atmosphere which excludes oxygen and moisture a slurry of (1) a porous inorganic oxide support material selected from the group consisting of silica, alumina, or a combination of silica and alumina, said support material containing not greater than about 5 millimoles of hydroxyl groups per gram of support material and a particle size not greater than about 10 microns and a surface area of from about 50 to about 800 m.sup.2 /g in an inert organic liquid medium; (B) mixing said slurry with (2) an alkoxide and stirring the resultant mixture at a temperature of from about -20.degree. C. to about 120.degree. C. for a time sufficient to saturate the surface of the support material; (C) mixing the product form (B) with (3) a titanium compound or a combination of a titanium compound and (4) a vanadium compound and stirring the resultant mixture at a temperature of from about -20.degree. C. to about 120.degree. C. for a time sufficient to allow complete reaction of the titanium compound and the vanadium compound with the organomagnesium moieties remaining on the solid support; (D) mixing the product from (C) with an inert organic solution of (5) a Group IIIA metal alkyl halide at a temperature of from about -20.degree. C. to about 120.degree. C. for a time sufficient to complete the reduction of the titanium and vanadium, if present, compounds to their final oxidation state.
    • 用于α-烯烃聚合的含过渡金属的催化剂通过以下步骤制备:(A)在惰性气氛中形成不含氧和水分的淤浆(1)多孔无机氧化物载体材料,其选自二氧化硅,氧化铝 ,或二氧化硅和氧化铝的组合,所述载体材料每克载体材料含有不大于约5毫摩尔羟基,粒度不大于约10微米,表面积为约50至约800平方米/ g在惰性有机液体介质中; (B)将所述浆料与(2)醇盐混合并在约-20℃至约120℃的温度下搅拌所得混合物足以使载体材料表面饱和的时间; (C)将产品形式(B)与(3)钛化合物或钛化合物和(4)钒化合物的组合混合并在约-20℃至约120℃的温度下搅拌所得混合物 在足以允许钛化合物和钒化合物与残留在固体载体上的有机镁部分完全反应的时间; (D)将来自(C)的产物与(5)IIIA族金属烷基卤的惰性有机溶液在约-20℃至约120℃的温度下混合足以完成还原的时间 的钛和钒(如果存在)化合物达到其最终氧化态。
    • 40. 发明授权
    • Olefin polymerization process for preparing high density or linear low
density polymers of controlled molecular weight distribution
    • 用于制备受控分子量分布的高密度或线性低密度聚合物的烯烃聚合方法
    • US5075271A
    • 1991-12-24
    • US609495
    • 1990-11-05
    • Nemesio D. Miro
    • Nemesio D. Miro
    • C08F4/685C08F10/00C08F10/02C08F110/02C08F210/16
    • C08F10/02C08F10/00C08F110/02C08F210/16
    • There is disclosed a catalyst composition for the polymerization of olefins, particularly alpha-olefins. The composition is prepared by synthesizing a catalyst precursor and then combining it with a conventional catalyst activator. The precursor is synthesized by: (a) contacting a solid, porous carrier with an aluminum compound; (b) contacting the resulting product with a mixture of vanadium and titanium compounds; (c) contacting the product with an alkyl ether and (d) pre-activating the product of step (c) with a mixture of a halogenating agent and an aluminum compound.The catalyst composition is used without a halogenating agent in the polymerization medium to produce narrow molecular weight distribution HDPE and LLDPE products, or with a halogenating agent in the polymerization medium to produce broad molecular weight distribution LLDPE and HDPE products.
    • 公开了用于烯烃聚合的催化剂组合物,特别是α-烯烃。 通过合成催化剂前体,然后将其与常规的催化剂活化剂组合来制备组合物。 前体是通过以下方法合成的:(a)使固体多孔载体与铝化合物接触; (b)使所得产物与钒和钛化合物的混合物接触; (c)使产物与烷基醚接触,和(d)用卤化剂和铝化合物的混合物预活化步骤(c)的产物。 催化剂组合物在聚合介质中不使用卤化剂使用,以在聚合介质中产生窄分子量分布HDPE和LLDPE产物,或与卤化剂一起产生宽分子量分布的LLDPE和HDPE产品。