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    • 2. 发明授权
    • Process for preparing low density ethylene copolymers
    • 制备低密度乙烯共聚物的方法
    • US4298713A
    • 1981-11-03
    • US106736
    • 1979-12-26
    • Yoshinori MoritaAkinori ToyotaNorio Kashiwa
    • Yoshinori MoritaAkinori ToyotaNorio Kashiwa
    • C08F2/00C08F2/04C08F2/06C08F4/00C08F4/60C08F4/64C08F210/00C08F210/16C08F297/08C08F4/16
    • C08F297/08C08F210/16Y10S526/904
    • A process for producing an ethylene copolymer having a density of from 0.900 to 0.945 g/cm.sup.3 by copolymerizing in two steps a predominant amount of ethylene with a minor amount of an alpha-olefin containing at least 3 carbon atoms at room temperature to not more than about 100.degree. C. under a pressure of about 1 to about 100 kg/cm.sup.2 in the presence of a catalyst composed of (A) a titanium catalyst component supported on a magnesium compound and (B) an organoaluminum compound; characterized in that said copolymerization is carried out in(i) a first step where about 0.01 to about 50 g, per gram of the titanium catalyst component (A), of the alpha-olefin containing at least 3 carbon atoms is polymerized, said catalyst further comprising an organic acid ester (C), and then(ii) a second step where the final product of ethylene copolymer is formed in an amount more than about 100 times the weight of the polymer formed in the first step.
    • 一种制备密度为0.900至0.945g / cm 3的乙烯共聚物的方法,通过在室温下将主要量的乙烯与少量含有至少3个碳原子的α-烯烃在两个步骤中共聚合成不超过 在(A)负载在镁化合物上的钛催化剂组分和(B)有机铝化合物组成的催化剂存在下,在约1至约100kg / cm2的压力下,约100℃。 其特征在于所述共聚在(i)第一步骤中进行,其中每克所述钛催化剂组分(A)中含有至少3个碳原子的α-烯烃聚合约0.01至约50g,所述催化剂 进一步包含有机酸酯(C),然后(ii)第二步,其中乙烯共聚物的最终产物的形成量大于第一步中形成的聚合物重量的约100倍。
    • 3. 发明授权
    • Process for polymerizing olefins and catalyst therefor
    • 聚合烯烃及其催化剂的方法
    • US4311817A
    • 1982-01-19
    • US183580
    • 1980-09-02
    • Yoshinori MoritaNorio Kashiwa
    • Yoshinori MoritaNorio Kashiwa
    • C08F4/00C08F4/60C08F4/64C08F10/00C08F4/16
    • C08F10/00Y10S526/908Y10S526/909
    • A process for polymerizing or copolymerizing an .alpha.-olefin in the presence of a catalyst composed of (A)' a transition metal catalyst component resulting from supporting a halogen-containing transition metal compound on spray-dried solid spherical particles of a magnesium compound and (B)' an organometallic compound of a metal of Groups I to III of the periodic table, wherein the transition metal catalyst component (A)' is a catalyst component (A) prepared by supporting the halogen-containing transition metal compound on solid spherical particles having a specific surface area of at least 20 m.sup.2 /g and an average particle diameter of 5 to 300.mu. obtained by spray-drying a suspension of an oxygen-containing, halogen-free magnesium compound having an average particle diameter of 0.01 to 20.mu., and a catalyst composition for use therein.
    • 在由(A)'由在镁化合物的喷雾干燥的固体球形颗粒上负载含卤素的过渡金属化合物得到的过渡金属催化剂组分的催化剂存在下,使α-烯烃聚合或共聚的方法和 B)'周期表第I至III族金属的有机金属化合物,其中过渡金属催化剂组分(A)'是通过将含卤素的过渡金属化合物负载在固体球形颗粒上制备的催化剂组分(A) 通过喷雾干燥平均粒径为0.01〜20μm的含氧无卤镁化合物的悬浮液而获得的比表面积为至少20m 2 / g,平均粒径为5〜300μm ,以及其中使用的催化剂组合物。
    • 4. 发明授权
    • Process for production of chemically blended composition of
non-elastomeric ethylene resins
    • 用于生产非弹性乙烯树脂的化学混合组合物的方法
    • US4307209A
    • 1981-12-22
    • US167141
    • 1980-07-09
    • Yoshinori MoritaNorio Kashiwa
    • Yoshinori MoritaNorio Kashiwa
    • C08F2/00C08F4/64C08F10/00C08F10/02C08F210/16C08F297/08C08L23/00C08L23/08
    • C08F297/08C08F10/00C08F10/02C08F210/16
    • In a process for the production of a chemically blended composition of non-elastomeric ethylene resins in a multiplicity of steps in the presence of a catalyst composed of a transition metal catalyst component and an organometallic compound, which comprises (a) a step of forming (i) an ethylene polymer or an ethylene/alpha-olefin copolymer having an alpha-olefin content of up to 15% by weight, said polymer or copolymer (i) having an intrinsic viscosity [.eta.] of 0.3 to 3, and (b) a step of forming (ii) an ethylene/alpha-olefin copolymer having an alpha-olefin content of 0.2 to 30% by weight which is more than that of the polymer or copolymer (i), said copolymer (ii) having an intrinsic viscosity [.eta.] of 1 to 12 which is at least 1.5 times that of the polymer or copolymer (i), said step (a) being performed first and then step (b) being performed in the presence of the product of step (a), or step (b) being performed first and then step (a) being performed in the presence of the product of step (b), the improvement wherein in steps (a) and (b), ethylene is polymerized or copolymerized with the alpha-olefin(1) in the presence of a catalyst composed of (A) a highly active titanium catalyst component containing titanium, magnesium and halogen and being capable of yielding an ethylene polymer in an amount of at least 250 g/millimole of a titanium atom.hr.kg/cm.sup.2 of ethylene pressure and (b) an organoaluminum compound,(2) so that the weight ratio of the polymer or copolymer (i) formed in step (a) to the copolymer (ii) formed in step (b) is (30-less than 60):(above 40-70), and(3) so that the resulting chemically blended composition has an intrinsic viscosity [.eta.] of 1 to 6 and an alpha-olefin content of 0.2 to 20% by weight.
    • 在由过渡金属催化剂组分和有机金属化合物组成的催化剂存在下,以多个步骤生产非弹性乙烯树脂的化学共混组合物的方法,其包括(a)形成( i)具有至多15重量%的α-烯烃含量的乙烯聚合物或乙烯/α-烯烃共聚物,所述聚合物或共聚物(i)的特性粘度η为0.3至3,和(b) 形成(ii)具有比聚合物或共聚物(i)的α-烯烃含量高0.2至30重量%的α-烯烃含量的乙烯/α-烯烃共聚物的步骤,所述共聚物(ii)具有特性粘度 1至12的η值为聚合物或共聚物(i)的至少1.5倍,所述步骤(a)首先进行,然后步骤(b)在步骤(a)的产物存在下进行, ,或者步骤(b)首先执行,然后步骤(a)在产品的存在下执行 步骤(b)的改进,其中在步骤(a)和(b)中,乙烯在由(A)高活性钛催化剂组分(A)组成的催化剂存在下与α-烯烃(1)聚合或共聚, 含有钛,镁和卤素并且能够产生至少250g /毫摩尔的钛原子的乙烯聚合物.hr.kg/cm 2的乙烯压力和(b)有机铝化合物,(2)使得 步骤(a)中形成的聚合物或共聚物(i)与步骤(b)中形成的共聚物(ii)的重量比为(30-小于60):(高于40-70),和(3) 所得到的化学共混组合物的特性粘度η为1至6,α-烯烃含量为0.2至20重量%。