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    • 3. 发明授权
    • Zieger-natta-type catalyst systems
    • 齐格纳塔型催化剂体系
    • US5166113A
    • 1992-11-24
    • US759980
    • 1991-09-17
    • Harald SchwagerPeter KoelleJuergen KerthRalf Zolk
    • Harald SchwagerPeter KoelleJuergen KerthRalf Zolk
    • C08F10/00
    • C08F10/00
    • Ziegler-Natta-type catalyst systems containing, as active constituents,a) a titanium-containing solid component which also contains magnesium, halogen and a carboxylic acid ester, and, as cocatalyst,b) an aluminum compound,wherein the carboxylic acid ester in the solid component is a diester of a carboxylic acid of the formula Ia or Ib ##STR1## where R.sup.1, R.sup.2, R.sup.3 and R.sup.4 are identical or different and are hydrogen, C.sub.1 - to C.sub.15 -alkyl, C.sub.7 - to C.sub.15 -alkylaryl, or 5- to 7-membered cycloalkyl, which may itself carry C.sub.1 - to C.sub.10 -alkyl groups, are particularly suitable for the preparation of polypropylene and copolymers of propylene containing minor amounts of other .alpha.,.beta.-unsaturated olefinic compounds having from 2 to 12 carbon atoms.
    • 含有作为活性成分的齐格勒 - 纳塔型催化剂体系a)含镁,卤素和羧酸酯的含钛固体组分,和作为助催化剂的b)铝化合物,其中羧酸酯在 固体组分是式Ia或Ib的羧酸的二酯(Ia)其中R 1,R 2,R 3和R 4相同或不同,为氢,C 1至C 15 - 烷基 可以自身携带C1-至C10烷基的C 7 -C 15烷基芳基或5-至7-元环烷基特别适用于制备聚丙烯和含有少量其它α,β- 具有2至12个碳原子的不饱和烯烃化合物。
    • 7. 发明授权
    • Preparation of homo- and copolymers of propene by means of a
Ziegler-Natta catalyst system
    • 通过齐格勒 - 纳塔催化剂体系制备丙烯的均聚物和共聚物
    • US5288824A
    • 1994-02-22
    • US934848
    • 1992-08-25
    • Juergen KerthRainer HemmerichPeter KoellePatrik Mueller
    • Juergen KerthRainer HemmerichPeter KoellePatrik Mueller
    • C08F4/658C08F4/02C08F4/60C08F4/647C08F4/652C08F10/00C08F10/06C08F4/64
    • C08F10/06
    • Polymers of propene are prepared using a Ziegler-Natta catalyst system comprising (1) titanium component which is based on a finely divided, shape-imparting silica gel and contains titan- ium, magnesium, chlorine and a benzenecarboxylic acid derivative, (2) an aluminum component and (3) a silane component. The process employs a titanium component (1) which is obtained by a method in which (1.1) first (I) a carrier is prepared from (Ia) a silica gel which has a relatively high moisture content, (Ib) an organomagnesium compound and (Ic) a gaseous chlorinating agent in a manner such that (1.1.1) first (Ia) is reacted with (Ib), (1.1.2) then (Ic) is passed into the mixture obtained from (1.1.1), (1.2) then a solid-phase intermediate is prepared from (I), (II) an alkanol, (III) titanium tetrachloride and (IV) a phthalic acid derivative in a manner such that (1.2.1) first (I) is reacted with (II), (1.2.2) then (III) is introduced into the mixture resulting from (1.2.1), with the proviso that (IV) is also introduced in (1.2.1) or (1.2.2), (1.3) then the solid-phase intermediate resulting from (1.2) is extracted with titanium tetrachloride or with a titanium tetrachloride/-hydrocarbon mixture and (1.4) finally the solid-phase product resulting from (1.3) is washed with a liquid hydrocarbon.
    • 使用齐格勒 - 纳塔催化剂体系制备丙烯聚合物,该催化剂体系包括(1)基于精细分散的形状赋予硅胶并含有钛,镁,氯和苯甲酸衍生物的钛组分,(2) 铝成分和(3)硅烷成分。 该方法采用通过以下方法得到的钛组分(1):其中(1.1)第一(I)载体由(Ia)由具有相对高的水分含量的硅胶制备,(Ib)有机镁化合物和 (Ic)气态氯化剂,使得(1.1.1)第一(Ia)与(Ib),(1.1.2)反应,然后(Ic)进入从(1.1.1)获得的混合物中, (1.2),然后以(I),(II)烷醇,(III)四氯化钛和(IV)邻苯二甲酸衍生物的方式制备固相中间体,使得(1.2.1)第一(I)为 与(II)反应,(1.2.2)然后将(III)引入由(1.2.1)得到的混合物中,条件是(IV)也引入(1.2.1)或(1.2.2) ,(1.3),然后用四氯化钛或四氯化钛/ - 烃混合物萃取由(1.2)得到的固相中间体,(1.4)最后将由(1.3)得到的固相产物用液体烃 。
    • 9. 发明授权
    • Phillips catalyst and its use for preparing ethylene homopolymers and
copolymers
    • 菲利普斯催化剂及其用于制备乙烯均聚物和共聚物的用途
    • US5324697A
    • 1994-06-28
    • US904924
    • 1992-06-26
    • Hans-Joachim MuellerRainer KonradGuenther SchweierSiegfried WeberRoland SaivePeter Koelle
    • Hans-Joachim MuellerRainer KonradGuenther SchweierSiegfried WeberRoland SaivePeter Koelle
    • C08F4/02C08F4/24C08F4/60C08F4/69C08F10/00C08F10/02
    • C08F10/02
    • A novel Phillips catalyst for the homopolymerization of ethylene and the copolymerization of ethylene with .alpha.-olefins contains as catalytically active components a specific chromium catalyst on an aluminum phosphate support and cocatalysts of the formula I to IV, ##STR1## where M is lithium, sodium and potassium,M.sup.1 is magnesium and zinc,M.sup.2 is boron and aluminum,R is C.sub.1 -C.sub.10 -alkyl and C.sub.6 -C.sub.20 -aryl,R.sup.1 is R and C.sub.1 -C.sub.10 -alkoxy and C.sub.6 -C.sub.20 -aryloxy,X is chlorine, bromine and iodine,n is 0, 1 and 2The chromium catalyst on an aluminum phosphate support can be obtained by applying chromium compounds to a finely divided aluminum phosphate with a P:A1 molar ratio near to or equal to 1 and a pore volume of >1 cm.sup.3 /g and activating the resulting intermediate at elevated temperatures in an oxidizing atmosphere. The novel Phillips catalyst has an exceptionally long duration of activity and its productivity can be increased further by adding hydrogen.
    • 用于乙烯均聚和乙烯与α-烯烃共聚的新型菲利普斯催化剂在磷酸铝载体上含有特定的铬催化剂和式I至IV的助催化剂,MR(I)M1R2(II)M2R3的催化活性组分 -n1Xn(III)MM2RR31(IV)其中M是锂,钠和钾,M1是镁和锌,M2是硼和铝,R是C1-C10-烷基和C6-C20-芳基,R1是R和C1- C10烷氧基和C6-C20芳氧基,X是氯,溴和碘,n是0,1和2。磷酸铝载体上的铬催化剂可以通过将铬化合物施加到具有P: A1摩尔比接近或等于1,孔体积> 1cm 3 / g,并在氧化气氛中在高温下活化所得中间体。 新型菲利普斯催化剂具有非常长的活性持续时间,并且通过加入氢可以进一步提高其生产率。