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    • 4. 发明授权
    • Preparation of a transition metal catalyst component for Ziegler
catalyst systems
    • 制备齐格勒催化剂体系的过渡金属催化剂组分
    • US4568659A
    • 1986-02-04
    • US666541
    • 1984-10-30
    • Volker WarzelhanRainer KarerRobert BachlGuido Funk
    • Volker WarzelhanRainer KarerRobert BachlGuido Funk
    • C08F4/02C08F4/62C08F4/64C08F4/68C08F10/00
    • C08F10/00
    • A transition metal catalyst component (1) for Ziegler catalyst systems is prepared by (1.1) first combining (1.1.1) an inorganic oxidic substance (I), as the carrier, with (1.1.2) a solution (II) consisting of (IIa) an organic solvent and (IIb) a transition metal composition to form a suspension (III), evaporating down this suspension to form a solid-phase intermediate (IV) and (1.2) then combining (1.2.1) the solid-phase intermediate (IV) obtained from (1.1) with (1.2.2) a solution of an organoaluminum compound (V) to form a suspension, the resulting suspended solid-phase products (VI) being the transition metal catalyst component (1).The characteristic feature is that the solution (II) employed in stage (1.1) consists of (IIa) a certain oxahydrocarbon and (IIb) a mixture of (IIb1) a vanadium trichloride/alcohol complex, (IIb2) a titanium trihalide and (IIb3) a zirconium tetrahalide.
    • 用于齐格勒催化剂体系的过渡金属催化剂组分(1)通过(1.1)首先将作为载体的无机氧化物质(I)与(1.1.2)由 (IIa)有机溶剂和(IIb)过渡金属组合物以形成悬浮液(III),将该悬浮液蒸发以形成固相中间体(IV)和(1.2),然后将(1.2.1) 由(1.1)与(1.2.2)得到的相变中间体(Ⅳ)与有机铝化合物(Ⅴ)的溶液形成悬浮液,得到的悬浮固相产物(Ⅵ)为过渡金属催化剂组分(ⅰ)。 特征在于,(1.1)中使用的溶液(II)由(IIa)某种氧杂烃和(IIb)(IIb1)三氯化钒/醇络合物,(IIb2)三卤化钛和(IIb3)的混合物 )四卤化锆。
    • 6. 发明授权
    • Preparation of a supported catalyst for the polymerization of
.alpha.-olefins
    • 制备用于α-烯烃聚合的负载型催化剂
    • US5455216A
    • 1995-10-03
    • US124047
    • 1993-09-21
    • Hans-Joachim MuellerGodofredo FollmerRainer KonradRoland SaiveMartin LuxHans-Helmut GoertzGuido Funk
    • Hans-Joachim MuellerGodofredo FollmerRainer KonradRoland SaiveMartin LuxHans-Helmut GoertzGuido Funk
    • C08F4/02C08F4/22C08F4/24C08F10/00B01J35/08B01J37/08
    • C08F10/00
    • A process for the preparation of a supported catalyst for the polymerization of .alpha.-olefins, in which(1) a silicon dioxide-containing support gel is prepared by(1.1) introducing a sodium water glass or potassium water glass solution into a swirling stream of an aqueous mineral acid longitudinally and tangentially to the stream, spraying the resultant silica hydrosol in drop form into a gaseous medium and allowing it to solidify to form a hydrogel, and freeing the resultant hydrogel from salts by washing without prior ageing,(1.2) drying the hydrogel resulting from (1.1) to form the support gel,(2) the support gel (1) is charged with chromium trioxide or a chromium compound which can be converted into chromium trioxide under the conditions of process step (3), giving a chromium-containing support gel, and(3) the chromium-containing support gel (2) is heated at from 400.degree. to 1100.degree. C. for from 10 to 1000 minutes in an anhydrous gas stream containing oxygen in a concentration of greater than 10% by volume,comprises drying the hydrogel resulting from step (1.1) in step (1.2) within a time of not more than 60 seconds in a shaping, high-speed dryer at an inlet temperature of from 80.degree. to 400.degree. C.
    • 一种制备用于α-烯烃聚合的负载催化剂的方法,其中(1)含二氧化硅的载体凝胶通过(1.1)将钠水玻璃或钾水玻璃溶液引入旋流 将水性无机酸纵向和切向于料流,将所得的二氧化硅水溶胶以液滴形式喷雾到气态介质中并使其固化形成水凝胶,并通过在没有预先熟化的情况下洗涤将所得水凝胶从盐中释放,(1.2)干燥 由(1.1)产生的形成支持凝胶的水凝胶,(2)载体凝胶(1)中加入三氧化铬或铬化合物,其可以在工艺步骤(3)的条件下转化为三氧化铬,得到 含铬载体凝胶,(3)含铬载体凝胶(2)在含有浓度浓度的氧的无水气流中在400〜1100℃下加热10〜1000分钟 大于10体积%包括在入口温度为80°至400°的成形高速干燥器中在不超过60秒的时间内将步骤(1.2)中由步骤(1.1)得到的水凝胶干燥 DEG C.
    • 9. 发明授权
    • Preparation of homopolymers of ethene and copolymers of ethene with
higher a-monoolefins using a Ziegler catalyst system
    • 使用齐格勒催化剂体系制备乙烯与乙烯共聚物与高级单环戊二烯的共聚物
    • US5210160A
    • 1993-05-11
    • US410047
    • 1989-09-19
    • Roland SaiveGuido FunkRainer Hemmerich
    • Roland SaiveGuido FunkRainer Hemmerich
    • C08F4/607C08F4/642C08F4/647C08F4/65C08F4/685C08F10/02
    • C08F10/02
    • Homopolymerization and copolymerization of ethene is carried out using a Ziegler catalyst system consisting of (1) a transition metal catalyst component, (2) an organoaluminum catalyst component and (3) an organohalogen catalyst component. The component (1) used is the solid-phase product (VI) which has been obtained by a method in which (1.1) first (1.1.1) an inorganic oxidic substance (I) as a carrier and (1.1.2) a solution (II) of (IIa) a certain oxahydrocarbon and (IIb) a mixture of (IIb1) a vanadium trichloride/alcohol complex and (IIb2) a titanium trihalide or titanium trihalide/alcohol complex and (IIc) a silicon or boron compound are combined with formation of a suspension (III) and the latter is evaporated to form a solid-phase intermediate (IV) and (1.2) then (1.2.1) the intermediate (IV) obtained in (1.1) and (1.2.2) a dissolved organoaluminum compound (V) are combined with formation of a suspension, the solid-phase product (VI) formed as the suspended substance being the transition metal catalyst component (1).
    • 使用由(1)过渡金属催化剂组分,(2)有机铝催化剂组分和(3)有机卤化物催化剂组分组成的齐格勒催化剂体系进行乙烯的均聚和共聚。 所使用的组分(1)是通过以下方法获得的固相产物(VI):(1.1)第一(1.1.1)作为载体的无机氧化物质(I)和(1.1.2)a (IIa)的某些氧杂烃的溶液(II)和(IIb)(IIb1)三氯化钒/醇络合物和(IIb2)三卤化钛或三卤化钛/醇络合物和(IIc)硅或硼化合物的混合物 (IV)和(1.2)然后(1.2.1)(1.1)和(1.2.2)中得到的中间体(Ⅳ),然后蒸发形成悬浮液(III) 将溶解的有机铝化合物(V)与形成悬浮液组合,形成为作为过渡金属催化剂组分(1)的悬浮物质的固相产物(VI)。
    • 10. 发明授权
    • Supported chromium oxide catalyst
    • 支持的氧化铬催化剂
    • US5164353A
    • 1992-11-17
    • US435681
    • 1989-11-14
    • Siegfried WeberGuido Funk
    • Siegfried WeberGuido Funk
    • C08F4/02C08F4/24C08F4/60C08F4/622C08F4/623C08F4/629C08F4/69C08F10/02
    • C08F10/02
    • A supported catalyst for ethene polymerization by Phillips catalysis is disclosed. The supported catalyst is prepared by (1) mixing a porous silicate in an inert, organic liquid to produce a silicate suspension, (2) providing an ester of phosphoric acid or phosphorous acid, (3) mixing an organic liquid, a chromium compound, and a trialkylaluminum compound to produce a chromium compound/aluminum compound and combining the silicate suspension, the phosphorus compound and the chromium compound/aluminum compound suspension. This resulting suspension is evaporated to dryness to form a catalyst intermediate. The catalyst intermediate is heated in nitrogen, then heated in an oxygen-containing atmosphere, and then heated again in nitrogen to produce an activated catalyst. The activated catalyst is suspended in an organic liquid and treated with an alkyl boron compound to produce the desired supported catalyst.
    • 公开了通过菲利普斯催化剂进行乙烯聚合的负载型催化剂。 负载型催化剂的制备方法是:(1)将惰性有机液体中的多孔硅酸盐混合以制备硅酸盐悬浮液,(2)提供磷酸或亚磷酸的酯,(3)将有机液体,铬化合物, 和三烷基铝化合物,以制备铬化合物/铝化合物并将硅酸盐悬浮液,磷化合物和铬化合物/铝化合物悬浮液混合。 将所得悬浮液蒸发至干,形成催化剂中间体。 将催化剂中间体在氮气中加热,然后在含氧气氛中加热,然后在氮气中再次加热以产生活化的催化剂。 将活化的催化剂悬浮在有机液体中并用烷基硼化合物处理以产生所需的负载型催化剂。