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    • 2. 发明授权
    • Process for the gas-phase polymerization of olefins
    • 烯烃气相聚合方法
    • US06228956B1
    • 2001-05-08
    • US08476063
    • 1995-06-07
    • Massimo CovezziPaolo GalliGabriele GovoniRoberto Rinaldi
    • Massimo CovezziPaolo GalliGabriele GovoniRoberto Rinaldi
    • C08F444
    • C08F10/00C08F210/16C08F4/6492C08F2/001
    • Process for the gas-phase polymerization of olefins of the formula CH2═CHR where R is hydrogen or an alkyl or aryl radical with 1 to 8 carbon atoms carried out in one or more reactors having a fluidized or mechanically agitated bed, using a catalyst obtained by reaction of a titanium halide or haloalcoholate and optionally an electron-donor compound supported on an active Mg-dihalide with an Al-trialkyl compound and optionally an electron-donor compound, comprising the steps of: a) contacting the catalyst components in the absence of polymerizable olefin or optionally in the presence of said olefin in an amount to from up to 3 g per g of solid catalyst component; b) prepolymerizing propylene or mixtures of propylene with ethylene or an alpha-olefin to form a propylene polymer having an insolubility in xylene of at least 60% by weight, in an amount of from 5 g of polymer per g of solid catalyst component to 10% by weight of the final catalyst yield; and c) polymerizing one or more CH2═CHR olefins in the gas phase in the presence of the prepolymer-catalyst system obtained in b), while maintaining in the gas phase an alkane in a molar concentration with respect to the total gases of from 20 to 90%.
    • 式CH 2 = CHR的烯烃的气相聚合方法,其中R是氢或具有1至8个碳原子的烷基或芳基,在具有流化床或机械搅拌床的一个或多个反应器中进行,使用获得的催化剂 通过卤化钛或卤代醇化物和任选的负载在活性二卤化镁上的电子给体化合物与Al-三烷基化合物和任选的电子给体化合物的反应,包括以下步骤:a)在不存在的情况下使催化剂组分接触 的可聚合烯烃或任选地在所述烯烃存在下的量为每克固体催化剂组分高达3克; b)将丙烯或丙烯与乙烯或α-烯烃的混合物预聚合以形成具有不溶性的丙烯聚合物 在二甲苯中至少60重量%,每克固体催化剂组分为5克聚合物至最终催化剂产率的10重量%; 在气相中,在b)中得到的预聚物 - 催化剂体系存在下,在气相中聚合一种或多种CH 2 = CHR烯烃,同时在气相中保持相对于总气体的摩尔浓度为20〜 90%。
    • 3. 发明授权
    • Process for the gas-phase polymerization of olefins
    • 烯烃气相聚合方法
    • US5733987A
    • 1998-03-31
    • US30654
    • 1993-03-12
    • Massimo CovezziPaolo GalliGabriele GovoniRoberto Rinaldi
    • Massimo CovezziPaolo GalliGabriele GovoniRoberto Rinaldi
    • C08F2/34C08F4/60C08F4/642C08F4/654C08F10/00C08F10/02
    • C08F10/02Y10S526/901
    • Process for the gas-phase polymerization of ethylene and ethylene mixtures with .alpha.-olefins CH.sub.2 .dbd.CHR in the presence of a high activity catalyst comprising a titanium compound containing at least one Ti-halogen bond, supported on magnesium dichloride in active form said process comprising the steps of: (a) contacting the catalyst component; (b) prepolymerizing ethylene or ethylene mixtures with .alpha.-olefins in order to produce a polymer amount of from approximately 5 g per g of solid component, up to an amount corresponding to about 10% of the final catalyst yield; (c) polymerizing ethylene or ethylene mixtures with .alpha.-olefins in the gas-phase, in the presence of the prepolymer-catalyst system obtained in (b), while maintaining in the gas phase a molar concentration concentration of the alkane comprised between 20 and 90% with respect to the total gases.
    • 在含活性形式负载在二氯化镁上的含有至少一个Ti-卤键的钛化合物的高活性催化剂存在下,用α-烯烃CH 2 = CHR气相聚合乙烯和乙烯混合物的方法,所述方法包括 步骤:(a)使催化剂组分接触; (b)将乙烯或乙烯混合物与α-烯烃预聚合,以产生约5g / g固体组分的聚合物量,至多相当于最终催化剂产率的约10%的量; (c)在(b)中获得的预聚物 - 催化剂体系的存在下,在气相中与α-烯烃聚合乙烯或乙烯混合物,同时在气相中保持烷烃的摩尔浓度浓度在20和 相对于总气体为90%。