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Highly active Ziegler type catalyst for ethylene (co)polymerisation

机译:用于乙烯(共)聚合的高活性齐格勒型催化剂

摘要

Ethylene opt. with other alpha-olefin in (co)polymerised in the presence of a catalyst system obtd. by bringing together in contact with one another (A) a reaction prod. (i) obtd. by reacting an intermediate reaction prod. (ii) obtd. by reaction of a hydropolysiloxane (I) with a Grignard reagent (II), with at least 1 nucleophilic reagent (III) chosen from an aldehyde, a ketone and an alcohol; (B) a transition metal cpd., and (C) at least 1 organoaluminium cpd. - High catalytic activity is obtd. even at a high temp. of at least 170 deg.C. Since the catalyst residue in polymer is minimised, the removal step may be omitted. Since the washing of the solid catalyst component prior to supplying it to the reactor is not required, the prepn. of the catalyst is simplified. EPAB- EP-101747 B A process for producing polyethylene which comprises polymerising ethylene ro copolymerizing ethylene with other alpha-olefin in the presence of a catalyst system obtained by bringing the following components (I) to (III) in contact with one another: (I) a reaction product (B) obtained by reacting an intermediate reaction product (A) obtained by a reaction of a hydropolysiloxane with a Grignard reagent, with at least one nucleophilic reagent selected from an aldehyde, a ketone and an alcohol, (II) a transition metal compound, and (III) at least one organic aluminium compound. USAB- US4657996 A Prodn. of polyethylene by: (co)polymerising ethylene in the presence of a catalyst system obtd. by bringing into contact (I) a reaction prod. obtd. by reacting an intermediate reaction prod. obtd. by reaction of a hydropolysiloxane with a Grignard reagent which is synthesised in the presence of an ether cpd. with at least one nucleophilic reagent, (II) a transition metal cpd., and (III) organo-Al cpd(s). - Pref. the Grignard reagent is MgR2 or MgRX; R is 1-12C hydrocarbon gp., X is halogen; and the molar ratio of MgR:Si is 1:1-5. - Pref. (II) is mixt. of Ti and V cpds; and (III) is of formula AlR1m(OR2)SX(3-m-S)i R1 and R2 are 1-12C hydrocarbon gps., X is halogen, and m, s and m+s are 0-3. - The (co)polymerisation is carried out at 30-300 deg. C.
机译:乙烯选择。与其他α-烯烃在催化剂体系存在下(共)聚合。通过使彼此接触(A)反应产物。 (i)。通过反应中间反应产物(ii)。通过使氢化聚硅氧烷(I)与格氏试剂(II)与至少一种选自醛,酮和醇的亲核试剂(III)反应; (B)过渡金属cpd。,和(C)至少一种有机铝cpd。 -高催化活性。即使在高温下至少170摄氏度由于使聚合物中的催化剂残留物最小化,因此可以省略去除步骤。由于不需要在将固体催化剂组分供应到反应器之前洗涤固体催化剂组分,因此该制备方法。催化剂的简化。 EPAB-EP-101747 BA的生产聚乙烯的方法,该方法包括在使以下组分(I)至(III)彼此接触而获得的催化剂体系的存在下,使乙烯与其他α-烯烃进行乙烯共聚合。 )通过使氢化聚硅氧烷与格氏试剂反应获得的中间反应产物(A)与至少一种选自醛,酮和醇的亲核试剂反应而获得的反应产物(B),过渡金属化合物,和(III)至少一种有机铝化合物。 USAB- US4657996 A产品通过在催化剂体系存在下(共)聚合乙烯来制备聚乙烯。通过使(I)反应产物接触。 t。通过反应中间反应产物t。通过使氢化聚硅氧烷与格氏试剂反应,该试剂在醚cpd的存在下合成。用至少一种亲核试剂,(II)过渡金属cpd。和(III)有机Al cpd。 -好格氏试剂为MgR2或MgRX; R为1-12C烃基,X为卤素; MgR∶Si的摩尔比为1∶1-5。 -好(二)混蛋。 Ti和V cpds的数量; (III)具有式AlR1m(OR2)SX(3-m-S)1 R 1和R 2是1-12C烃基gps。X是卤素,并且m,s和m + s是0-3。 -(共)聚合在30-300℃下进行。 C。

著录项

  • 公开/公告号ES8602854A1

    专利类型

  • 公开/公告日1986-03-16

    原文格式PDF

  • 申请/专利权人 NISSAN CHEMICAL INDUSTRIES LTD;

    申请/专利号ES19830528061

  • 发明设计人

    申请日1983-12-14

  • 分类号C08F4/62;C08F10/02;

  • 国家 ES

  • 入库时间 2022-08-22 07:37:39

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