首页> 外国专利> Ziegler-Natta type catalyst system for polymerising propylene¨ - is based on solid component from titanium cpd., magnesium organo-oxy halide, halogen and carboxylic acid deriv., with aluminium cpd.

Ziegler-Natta type catalyst system for polymerising propylene¨ - is based on solid component from titanium cpd., magnesium organo-oxy halide, halogen and carboxylic acid deriv., with aluminium cpd.

机译:用于聚合丙烯的Ziegler-Natta型催化剂体系,是基于钛cpd,有机氧卤化镁,卤素和羧酸衍生物以及铝cpd的固体成分。

摘要

System (I) is based on (A) Ti-contg. solid component contg. (A1) Ti-cpd. (A2) Mg cpd. of formula Mg(OR1)X R1 = 1-10C alkyl, 6-10 C aryl, or alkylaryl or 5-7 membered cycloalkyl, opt. contg. 1-4C alkyl gps. X = Cl or Br, (A3) halogen (A4) carboxylic acid derivs. (B) Al cpd. and opt. (C) other electron donor cpds. Also claimed are (i) prepn. of (I) by (1) suspending finely divided carrier material in (II) in liq. alkane at 10-120 deg.C. (2) treating suspension with 0.1-10 M soln. of (A2) in liq. alkane (3) adding to this mixt. after 30-120 minutes at 10-150 deg.C 0.2-5 mol halogen or hydrogen halide per mol. Mg of (A2) (4) after 60-300 minutes treating reaction prod. at 10-150 deg.C with per mol. Mg 0.1-5 mol 1-8C alkanol 1-20 mol halide or alcoholate of 3- or 4-valent Ti and 0.01-1 mol. (A4), (5) filtering off solid (I) and washing (I) with liq. alkane, and (ii) prepn. of polymers (III) of propylene (IV) by polymerisation at 20-150 deg.C and 1-100 bar using (I). USE/ADVANTAGE - Prodn. of (IV) homopolymers and copolymers with minor amts. of other 2-12C alpha, beta-unsatd. olefinic cpds. (I) have higher productivity and improved stereospecificity partic. in gas phase polymerisation, (III) have very small proportion of fines (less than 0.2mm) low Cl content, and good mechanical properties. (6pp Dwg.No.0/0)
机译:系统(I)基于(A)Ti-contg。固体成分续(A1)Ti-cpd。 (A2)镁cpd式Mg(OR1)X R1 = 1-10C烷基,6-10C芳基或烷基芳基或5-7元环烷基的基团。续1-4C烷基gps。 X = Cl或Br,由(A3)卤素(A4)羧酸衍生。 (B)Al cpd。并选择。 (C)其他电子给体cpds。还要求保护(i)prepn。通过(1)将细碎的载体材料悬浮在(II)中的液体中。 10-120℃下的烷烃。 (2)用0.1-10 M溶液处理悬浮液。 (A2)的液体。烷烃(3)添加到该混合物中。在10-150℃下30-120分钟后,每摩尔0.2-5摩尔卤素或卤化氢。处理反应产物60-300分钟后的(A2)(4)的镁。在10-150℃与每摩尔镁0.1-5摩尔1-8C烷醇1-20摩尔3或4价钛和0.01-1摩尔的卤化物或醇化物。 (A4),(5)滤出固体(I)并用液洗涤(I)。烷和(ii)制备。通过使用(I)在20-150℃和1-100bar下聚合,制备丙烯(IV)的聚合物(III)。使用/优势-产品(IV)均聚物和少量胺的共聚物。其他2-12C alpha(无β)。烯烃cpds。 (一)具有更高的生产率和改善的立体定向性。在气相聚合中,(III)的细粉比例非常小(小于0.2mm),且Cl含量低,并且具有良好的机械性能。 (6pp Dwg.No.0 / 0)

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