会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 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。
    • 2. 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。
    • 4. 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.
    • 5. 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.
    • 7. 发明授权
    • Preparation of homopolymers of ethylene or copolymers of ethylene
    • 制备乙烯均聚物或乙烯共聚物
    • US5414064A
    • 1995-05-09
    • US274692
    • 1994-07-14
    • Martin LuxGuido FunkRoland SaiveHans-Helmut GoertzRainer Konrad
    • Martin LuxGuido FunkRoland SaiveHans-Helmut GoertzRainer Konrad
    • C09K3/16C08F2/34C08F2/44C08F10/00C08F10/02C08F110/02C08K5/17C08K5/20C08L23/02
    • C08F10/02C08F110/02Y10S526/901Y10S526/904
    • Homopolymers of ethylene or copolymers of ethylene with minor amounts of other C.sub.3 -C.sub.12 -alk-1-enes are prepared by catalytic polymerization in a suspension or in the gas phase in the presence of an antistatic agent at from 50 to 120.degree. C. and from 5 to 50 bar by a process in which the antistatic agent used is a mixture of the following substances:a) a metal salt of medialanic acid of the formula (I) ##STR1## b) a metal salt of an anthranilic acid of the general formula (II) ##STR2## where the organic radical R.sup.1 is either.alpha.)--CO--(CH.sub.2).sub.x --CH.sub.3 (II.alpha.)or.beta.)--CO--(CH.sub.2).sub.y --CH.dbd.CH--(CH.sub.2).sub.z --CH.sub.3(III.beta.)and x, y and z are each an integer and are from 6 to 18 for x, from 1 to 16 for y, from 1 to 16 for z and from 4 to 17 for y+z, andc) a polyamine obtainable by reacting epichlorohydrin and an aliphatic primary monoamine or an N-alkylalkylenediamine of the general formula (IV)R.sup.2 NH--R.sup.3 --NH.sub.2 (IV),whereR.sup.2 is C.sub.8 -C.sub.24 -alkyl andR.sup.3 is C.sub.2 -C.sub.6 -alkylene.
    • 乙烯均聚物或乙烯与少量其它C 3 -C 12烷-1-烯的共聚物通过在50至120℃的抗静电剂存在下在悬浮液或气相中催化聚合制备,以及 使用的抗静电剂为以下物质的混合物的方法为5〜50巴:a)式(I)的中间体金属盐(a)b)邻氨基苯甲酸的金属盐 通式(II)的酸其中有机基团R1是α)-CO-(CH2)x-CH3(IIa)或β)-CO-(CH2)y-CH = CH - (CH 2)z -CH 3(IIIβ),x,y和z各自为整数,x为6至18,y为1至16,z为1至16,y为4至17 + z,和c)通过使表氯醇和通式(IV)R 2 NH-R 3 -NH 2(IV)的脂族伯单胺或N-烷基亚烷基二胺反应得到的多胺,其中R 2是C 8 -C 24 - 烷基,R 3是C 2 -C 6-亚烷基。
    • 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
    • Preparation of homopolymers of ethene and copolymers of ethene with high
.alpha.-monoolefins using a Ziegler catalyst system
    • 使用齐格勒催化剂体系制备高(ALPHA) - 烯烃的乙烯和乙烯共聚物的共聚物
    • US5112928A
    • 1992-05-12
    • US416410
    • 1989-10-03
    • Roland SaiveGuido FunkRobert Bachl
    • Roland SaiveGuido FunkRobert Bachl
    • C08F4/68C08F10/00
    • C08F10/00
    • The homopolymerization and copolymerization of ethene are 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.In the homopolymerization or copolymerization, the solid-phase product (VI) used as (1) is the product which has been obtained by a method in which (1.1) first (1.1.1) an inorganic oxidic substance (I) as the carrier and (1.1.2) a solution (II) of (IIa) a certain oxahydrocarbon and (IIb) a vanadium trichloride/alcohol complex and (IIc) a silicon or boron compound are combined with formation of a suspension (III), the latter is evaporated down 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 the formation of a suspension, the solid-phase product (VI) obtained 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。 在均聚或共聚时,用作(1)的固相产物(VI)是通过以下方法获得的产物:其中(1.1)第一(1.1.1)无机氧化物质(I)作为载体 和(1.1.2)(IIa)(IIa)的某种氧杂烃和(IIb)三氯化钒/醇络合物和(IIc)硅或硼化合物的溶液(II)与形成悬浮液(III) 蒸发掉形成固相中间体(Ⅳ),然后(1.2)然后(1.2.1)将(1.1)和(1.2.2)中得到的中间体(Ⅳ)溶解的有机铝化合物(Ⅴ)与 形成悬浮液时,作为悬浮物质得到的固相物(VI)为过渡金属催化剂成分(1)。