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    • 2. 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。
    • 3. 发明授权
    • Preparation of homopolymers and copolymers of ethene by Phillips
catalysis
    • 通过菲利普斯催化制备乙烯的均聚物和共聚物
    • US4727124A
    • 1988-02-23
    • US047116
    • 1987-05-08
    • Rainer KonradRudolf Mueller-MallGuenther Schweier
    • Rainer KonradRudolf Mueller-MallGuenther Schweier
    • C08F2/06C08F4/02C08F4/22C08F4/24C08F4/62C08F4/64C08F10/00C08F10/02C08F2/24
    • C08F10/00C08F2410/01
    • Ethane polymers are prepared by Phillips catalysis using (1) a supported catalyst which is laden with chromium, phosphorus and titanium and (2) a cocatalyst, (1) being obtained by a procedure in which (1.1) a catalyst intermediate laden with chromium, phosphorus and titanium is prepared from a silicate carrier, a selected chromium compound, a selected phosphorus compound and a selected titanium compound, and (1.2) the catalyst intermediate is then heated in an oxygen-containing gas stream. In the process, the supported catalyst (1) used is one which is obtained (using specific methods and substances in each case) by a procedure in which (1.1) in a first stage (1.1.1), a suspension is first prepared from (1.1.1.1) a finely divided silicate carrier and (1.1.1.2) an inert organic solvent, (1.1.2) a suspension is then prepared from (1.1.2.1) a finely divided chromium trioxide and (1.1.2.2) an inert organic solvent, (1.1.3) thereafter (1.1.3.1) the suspension resulting from (1.1.2) is combined with (1.1.3.2) a phosphate or phosphite, (1.1.4) then (1.1.4.1) the suspension obtained from (1.1.1) is combined with (1.1.4.2) the reaction product obtained in (1.1.3), (1.1.5) thereafter (1.1.5.1) the suspension formed in (1.1.4) is combined with (1.1.5.2) a titanate, (1.1.6) finally the suspension obtained in (1.1.5) is evaporated to dryness and then (1.2) in a second stage, (1.2.1) the intermediate obtained in (1.1) is first treated with a nitrogen stream, (1.2.2) an intermediate obtained in (1.2.1) is then heated in an oxygen-containing gas stream and finally (1.2.3) the intermediate obtained in (1.2.2) is treated with a nitrogen stream, and a lithiumalkyl is used as (2).
    • 通过使用(1)载有铬,磷和钛的载体催化剂和(2)助催化剂的菲尼普斯催化剂制备乙烷聚合物,(1)通过以下程序获得,其中(1.1)载有铬的催化剂中间体, 磷和钛由硅酸盐载体,选择的铬化合物,选择的磷化合物和选择的钛化合物制备,然后在含氧气流中加热催化剂中间体。 在该方法中,使用的负载催化剂(1)是通过第一阶段(1.1.1)中的(1.1)的步骤获得的(使用具体方法和每种情况下的物质),悬浮液首先由 (1.1.1.1)细碎的硅酸盐载体和(1.1.1.2)惰性有机溶剂,(1.1.2)悬浮液然后由(1.1.2.1)细碎的三氧化铬和(1.1.2.2)惰性的 有机溶剂(1.1.3)(1.1.3.1)将得自(1.1.2)的悬浮液与(1.1.3.2)磷酸酯或亚磷酸酯(1.1.4)然后(1.1.4.1)合并得到的悬浮液 (1.1.1)与(1.1.4)中得到的反应产物(1.1.3),(1.1.5)(1.1.5.1)中合并(1.1.4),将(1.1.4)中形成的悬浮液与(1.1 0.5.2)钛酸盐(1.1.6)最后,将(1.1.5)中得到的悬浮液在第二阶段蒸发至干,然后(1.2)(1.2.1),首先处理(1.1)中获得的中间体 用氮气流(1.2.2)中间体 然后在含氧气流中加热(1.2.1),最后(1.2.3)用氮气流处理(1.2.2)中得到的中间体,使用烷基锂作为(2)。
    • 4. 发明授权
    • Preparation of homopolymers and copolymers of ethene by Phillips
catalysis
    • 通过菲利普斯催化制备乙烯的均聚物和共聚物
    • US4728703A
    • 1988-03-01
    • US28651
    • 1987-03-20
    • Rainer KonradVolker WarzelhanHans GropperGuenther Schweier
    • Rainer KonradVolker WarzelhanHans GropperGuenther Schweier
    • C08F2/24C08F4/22C08F10/02
    • C08F10/02C08F2410/01
    • Ethene polymers are prepared by Phillips catalysis using (1) a supported catalyst which is loaded with chromium and titanium and (2) a co-catalyst, (1) having been obtained by preparing (1.1) a chromium- and titanium-loaded catalyst intermediate from (1.1.a) a silicate carrier material, (1.1.b) a selected chromium compound and (1.1.c) a selected titanium compound and then (1.2) heating said catalyst intermediate in an oxygen-containing gas stream, the (1) used having been obtained by, in general terms, (1.1) preparing in the first stage (1.1.1) a suspension from (1.1.1.1) a finely divided silicate carrier material and (1.1.1.2) a liquid alkane, (1.1.2) then (1.1.2.1) combining the suspension resulting from (1.1.1.) with (1.1.2.2.) a finely divided chromium trioxide, (1.1.3) thereupon (1.1.3.1) combining the suspension obtained from (1.1.2) with (1.1.3.2) an alkanol, (1.1.4) thereafter (1.1.4.1) combining the suspension formed in (1.1.3) with (1.1.4.2) a titanium compound of the formula Ti(OR).sub.4, where R is alkyl, aryl or cycloalkyl, and (1.1.5) finally evaporating the suspension obtained in (1.1.4) to dryness, and then (1.2) in the second stage first (1.2.1) treating the catalyst intermediate obtained in the first state (1.1) with a nitrogen stream, thereupon (1.2.2) heating the intermediate obtained in (1.2.1) in an oxygen-containing gas stream, and finally (1.2.3) treating the intermediate obtained in (1.2.2) with a nitrogen stream; and as (2) with an alkyllithium.
    • 通过菲利普斯催化法,使用(1)载有铬和钛的载体催化剂和(2)助催化剂制备乙烯聚合物,(1)通过制备(1.1)载有铬和钛的催化剂中间体 从(1.1.a)硅酸盐载体材料,(1.1b)选择的铬化合物和(1.1.c)所选择的钛化合物,然后(1.2)在含氧气流中加热所述催化剂中间体,(1 )(1.1)在第一阶段(1.1.1)中制备了(1.1.1.1)细分硅酸盐载体材料和(1.1.1.2)液体烷烃(1.1 (1.1.2.1)将由(1.1.1。)得到的悬浮液与(1.1.2.2。)细碎的三氧化铬(1.1.3)(1.1.3.1)组合,得到的悬浮液 1.1.2)与(1.1.3.2)链烷醇(1.1.4)(1.1.4.1)将(1.1.3)中形成的悬浮液与(1.1.4.2)结合形成式 Ti(OR)4,其中R是烷基,芳基或环烷基,和(1.1.5)最终将(1.1.4)中得到的悬浮液蒸发至干,然后在第二阶段(1.2.1)中蒸发(1.2) 用氮气流处理在第一状态(1.1)中获得的催化剂中间体,随后(1.2.2)在含氧气流中加热(1.2.1)中获得的中间体,最后(1.2.3)处理 (1.2.2)中获得的中间体与氮气流; 和(2)与烷基锂反应。
    • 5. 发明授权
    • Preparation of homopolymers and copolymers of ethene by Phillips
catalysis
    • 通过菲利普斯催化制备乙烯的均聚物和共聚物
    • US4814308A
    • 1989-03-21
    • US110872
    • 1987-10-21
    • Rainer KonradGuido FunkJuergen Schmidt-ThuemmesRudolf Mueller-MallGuenther Schweier
    • Rainer KonradGuido FunkJuergen Schmidt-ThuemmesRudolf Mueller-MallGuenther Schweier
    • C08F4/02C08F4/24C08F4/48C08F4/62C08F10/02
    • C08F10/02
    • Ethene polymerization by Phillips catalysis is carried out using (1) a supported catalyst, which is laden with chromium, phosphorus and aluminum, and (2) a cocatalyst, (1) being obtained by a method in which (1.1) a catalyst intermediate laden with chromium, phosphorus and aluminum is prepared from a silicate carrier, a selected chromium compound, a selected phosphorus compound and a selected aluminum compound, and then (1.2) the catalyst intermediate is heated in an oxygen-containing gas stream. In this process, the component (1) used is one which is obtained by a method in which, in each case in a specific manner, (1.1) in a first stage, (1.1.1) first a suspension is prepared from (1.1.1.1) a finely divided silicate carrier and (1.1.1.2) an inert organic solvent, (1.1.2) then, (1.1.2.1) in an inert organic solvent, (1.1.2.2) an organic chromium compound is combined with (1.1.2.3) an aluminum trialkyl, (1.1.3) then (1.1.3.1) the suspension resulting from (1.1.1) is combined with (1.1.3.2) a phosphoric acid or phosphite and (1.1.3.3) the product obtained from (1.1.2), (1.1.4) finally, the suspension obtained in (1.1.3) is evaporated to dryness, and then (1.2) in a second stage, first (1.2.1) the intermediate obtained from (1.1) is treated with a stream of nitrogen, then (1.2.2) the intermediate obtained from (1.2.1) is heated in an oxygen-containing gas stream, and finally (1.2.3) the intermediate obtained from (1.2.2) is treated with a stream of nitrogen, and both a lithiumalkyl and a boronalkyl are used as (2).
    • 通过菲利普斯催化进行的乙烯聚合使用(1)负载催化剂,其载有铬,磷和铝,和(2)助催化剂,(1)通过以下方法获得:(1)将载体催化剂中间体 由硅酸盐载体,选择的铬化合物,选择的磷化合物和选择的铝化合物制备铬,磷和铝,然后(1.2)在含氧气流中加热催化剂中间体。 在该方法中,所使用的组分(1)是通过在每种情况下以具体方式(1.1)在第一阶段(1.1.1)中首先从(1.1)制备悬浮液的方法获得的组分 .1.1)精细分散的硅酸盐载体和(1.1.1.2)惰性有机溶剂(1.1.2)然后,(1.1.2.1)在惰性有机溶剂(1.1.2.2)中将有机铬化合物与( 1.1.2.3)三烷基铝(1.1.3)然后(1.1.3.1)将由(1.1.1)得到的悬浮液与(1.1.3.2)磷酸或亚磷酸酯和(1.1.3.3)得到的产物 从(1.1.2),(1.1.4)最终得到的(1.1.3)中得到的悬浮液蒸发至干,然后在第二阶段(1.2)中,首先(1.2.1)从(1.1 )用氮气流处理,然后(1.2.2)从(1.2.1)获得的中间体在含氧气流中加热,最后(1.2.3)从(1.2.2)得到的中间体 用氮气流和二氧化钛处理 和硼烷基用作(2)。
    • 7. 发明授权
    • Phillips catalyst and its use for the preparation of
ethylene/alpha-olefin copolymers
    • 菲利普斯催化剂及其用于制备乙烯/α-烯烃共聚物的用途
    • US5480852A
    • 1996-01-02
    • US247479
    • 1994-05-23
    • Hans-Joachim MuellerKaspar EvertzSiegfried WeberGuido FunkRainer KonradRoland Saive
    • Hans-Joachim MuellerKaspar EvertzSiegfried WeberGuido FunkRainer KonradRoland Saive
    • C08F2/42C08F4/00C08F4/02C08F4/06C08F4/22C08F4/24C08F10/00C08F10/02B01J27/182
    • C08F10/00
    • A novel Phillips catalyst for the copolymerization of ethylene with .alpha.-olefins, contains, as a catalytically active component, a finely divided, aluminum silicate-supported, phosphorus-containing chromium catalyst. This can be prepared by applying at least one organic phosphorus(III), (IV) and/or (V) compound and at least one chromium(III) compound which does not react with said phosphorus compounds under the reaction conditions used, in succcession in any order or simultaneously, to a finely divided aluminum silicate hydrogel or xerogel with formation of a catalyst intermediate and activating the catalyst intermediate at elevated temperatures in an oxidizing atmosphere, with the result that the chromium catalyst is formed. The novel Phillips catalyst gives ethylene/.alpha.-olefin copolymers in which the comonomers are more uniformly distributed over the copolymer chains than is the case with ethylene/.alpha.-olefin copolymers which have been prepared with the aid of conventional Phillips catalysts. Moldings which have been produced from the ethylene/.alpha.-olefin copolymers obtained in the novel procedure have a particularly high environmental stress cracking resistance and an excellent creep rupture strength.
    • 用于乙烯与α-烯烃共聚的新颖的菲利普斯催化剂包含作为催化活性组分的细碎的含硅酸铝载体的含磷的铬催化剂。 这可以通过在所用的反应条件下施用至少一种不与所述磷化合物反应的有机磷(III),(IV)和/或(V)化合物和至少一种铬(III)化合物来制备, 以任何顺序或同时的方式,在形成催化剂中间体的细分的硅酸铝水凝胶或干凝胶中,并在氧化气氛中在高温下活化催化剂中间体,结果形成铬催化剂。 新型菲利普斯催化剂提供了乙烯/α-烯烃共聚物,其中共聚单体比共聚物链更均匀地分布在使用常规菲利普斯催化剂制备的乙烯/α-烯烃共聚物的情况下。 由新方法得到的乙烯/α-烯烃共聚物制成的成型品具有特别高的耐环境应力开裂性和优异的抗蠕变断裂强度。
    • 8. 发明授权
    • Phillips catalyst and its use for the preparation of
ethylene/.alpha.-olefin copolymers
    • 菲利普斯催化剂及其在制备乙烯/α-烯烃共聚物中的应用
    • US5557021A
    • 1996-09-17
    • US512556
    • 1995-08-08
    • Hans-Joachim MuellerKaspar EvertzSiegfried WeberGuido FunkRainer KonradRoland Saive
    • Hans-Joachim MuellerKaspar EvertzSiegfried WeberGuido FunkRainer KonradRoland Saive
    • C08F2/42C08F4/00C08F4/02C08F4/06C08F4/22C08F4/24C08F10/00C08F10/02C07C2/24
    • C08F10/00
    • A novel Phillips catalyst for the copolymerization of ethylene with .alpha.-olefins, contains, as a catalytically active component, a finely divided, aluminum silicate-supported, phosphorus-containing chromium catalyst. This can be prepared by applying at least one organic phosphorus(III), (IV) and/or (V) compound and at least one chromium(III) compound which does not react with said phosphorus compounds under the reaction conditions used, in succcession in any order or simultaneously, to a finely divided aluminum silicate hydrogel or xerogel with formation of a catalyst intermediate and activating the catalyst intermediate at elevated temperatures in an oxidizing atmosphere, with the result that the chromium catalyst is formed. The novel Phillips catalyst gives ethylene/.alpha.-olefin copolymers in which the comonomers are more uniformly distributed over the copolymer chains than is the case with ethylene/.alpha.-olefin copolymers which have been prepared with the aid of conventional Phillips catalysts. Moldings which have been produced from the ethylene/.alpha.-olefin copolymers obtained in the novel procedure have a particularly high environmental stress cracking resistance and an excellent creep rupture strength.
    • 用于乙烯与α-烯烃共聚的新颖的菲利普斯催化剂包含作为催化活性组分的细碎的含硅酸铝载体的含磷的铬催化剂。 这可以通过在所用的反应条件下施用至少一种不与所述磷化合物反应的有机磷(III),(IV)和/或(V)化合物和至少一种铬(III)化合物来制备, 以任何顺序或同时的方式,在形成催化剂中间体的细分的硅酸铝水凝胶或干凝胶中,并在氧化气氛中在高温下活化催化剂中间体,结果形成铬催化剂。 新型菲利普斯催化剂提供了乙烯/α-烯烃共聚物,其中共聚单体比共聚物链更均匀地分布在使用常规菲利普斯催化剂制备的乙烯/α-烯烃共聚物的情况下。 由新方法得到的乙烯/α-烯烃共聚物制成的成型品具有特别高的耐环境应力开裂性和优异的抗蠕变断裂强度。
    • 9. 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.
    • 10. 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
    • US5625013A
    • 1997-04-29
    • US422937
    • 1995-05-24
    • Hans-Joachim MuellerGodofredo FollmerRainer KonradRoland SaiveMartin LuxHans-Helmut GoertzGuido Funk
    • Hans-Joachim MuellerGodofredo FollmerRainer KonradRoland SaiveMartin LuxHans-Helmut GoertzGuido Funk
    • C08F4/02C08F4/22C08F4/24C08F10/00B01J35/08
    • 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.