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    • 3. 发明授权
    • Modified chromium-containing catalyst composition for polymerizing
olefins and method of preparing the catalyst composition
    • 用于聚合烯烃的改性含铬催化剂组合物及其制备方法
    • US5006506A
    • 1991-04-09
    • US454538
    • 1989-12-21
    • John T. T. HsiehAnn L. Pruden
    • John T. T. HsiehAnn L. Pruden
    • B01J23/26C08F4/24C08F10/00
    • B01J23/26C08F10/00
    • A modified supported catalyst composition for polymerizing olefins, particularly alpha-olefins, for example, ethylene or ethylene and 1-hexane, is prepared by combining a chromium compound-containing catalyst with a modifier which is an oxide of an element of Group IIIA of the Periodic Table of the Elements. The modifier contains a small quantity of water. The resulting modified catalyst composition produces polymer resins having higher values of High Load Melt Index -HLMI (I.sub.21) than catalyst compositions without the modifier.There is also disclosed a process for polymerizing olefins, at relatively lower temperatures than was heretofore possible, to obtain resins of relatively high HLMI, using the above-identified modified catalyst composition. The resulting polymers can be used for the fabrication of blow-molded products, e.g., household and industrial containers.
    • 通过将含铬化合物的催化剂与作为IIIA族元素的氧化物的改性剂组合来制备用于聚合烯烃,特别是α-烯烃,例如乙烯或乙烯和1-己烷的改性负载型催化剂组合物 元素周期表。 改性剂含有少量的水。 得到的改性催化剂组合物产生的聚合物树脂具有比没有改性剂的催化剂组合物更高的高负荷熔体指数-HLMI值(I21)。 还公开了使用上述改性的催化剂组合物在相对较低的温度下聚合烯烃的方法,以获得相对高的HLMI的树脂。 所得聚合物可用于制造吹塑成型产品,例如家用和工业容器。
    • 4. 发明授权
    • Polymerization catalyst
    • 聚合催化剂
    • US4435518A
    • 1984-03-06
    • US444287
    • 1982-11-24
    • B. Timothy PenningtonPaul V. RolingJohn T. T. Hsieh
    • B. Timothy PenningtonPaul V. RolingJohn T. T. Hsieh
    • C08F4/00C08F2/34C08F4/60C08F4/68C08F10/00
    • C08F10/00Y10S526/901
    • Catalyst compositions which are particularly useful for the preparation of ethylene polymers having a narrow molecular weight distribution are obtained by (1) drying an inorganic oxide having surface hydroxyl groups, e.g., silica, alumina, magnesia, etc., to remove adsorbed water, (2) reacting the surface hydroxyl groups with at least a stoichiometric amount of an organometallic compound having at least one alkyl group attached to a Group III metal, e.g., a trialkylaluminum, (3) reacting the thus-treated inorganic oxide with a vanadium halide, such as (a) VOCl.sub.3, VOBr.sub.3, and/or mono-, di-, and/or trihydrocarbyloxy derivatives thereof and/or (b) VCl.sub.4, VBr.sub.4, and/or mono-, di-, tri-, and/or tetrahydrocarbyloxy derivatives thereof, and (4) reacting that reaction product with at least about 0.1 mol, per mol of organometallic compound, of an alcohol containing 1 to 18 carbon atoms.
    • 特别可用于制备具有窄分子量分布的乙烯聚合物的催化剂组合物通过以下方法获得:(1)干燥具有表面羟基的无机氧化物,例如二氧化硅,氧化铝,氧化镁等,以去除吸附的水( 2)使表面羟基与至少一种化学计量量的具有至少一个与III族金属连接的烷基的有机金属化合物反应,例如三烷基铝,(3)使经过处理的无机氧化物与卤化钒反应, 例如(a)VOCl 3,VOBr 3和/或其单 - ,二 - 和/或三氢氧羰基衍生物和/或(b)VCl4,VBr4和/或单 - ,二 - ,三 - 和/ 其衍生物,和(4)使该反应产物与每摩尔有机金属化合物至少约0.1摩尔含有1至18个碳原子的醇反应。
    • 5. 发明授权
    • High efficiency catalyst for high bulk density polyethylene
    • 高密度聚乙烯的高效催化剂
    • US4288578A
    • 1981-09-08
    • US34114
    • 1979-04-30
    • John T. T. Hsieh
    • John T. T. Hsieh
    • C08F10/02C08F4/02
    • C08F10/02
    • A unique high efficiency catalyst for the polymerization of alpha-olefins has been developed based on the use of methanol treated magnesium oxide as support, an equimolar mixture of titanium tetrachloride and tetrabutyltitanate as titanium source impregnated on the support, and an organoaluminum compound as reducing agent. The polyethylene produced by this catalyst has narrow molecular weight distribution, high bulk density, high melt index, and minimum catalyst residue due to the high polymer to catalyst ratio. The copolymers produced by this catalyst have narrow molecular weight distribution, but have lower bulk density, low melt index and low density.
    • 已经开发了用于α-烯烃聚合的独特的高效催化剂,其基于使用甲醇处理的氧化镁作为载体,将四氯化钛和四丁基钛酸四丁酯作为浸渍在载体上的钛源的等摩尔混合物和作为还原剂的有机铝化合物 。 由于该聚合物与催化剂的比例高,由该催化剂生产的聚乙烯具有窄的分子量分布,高堆积密度,高熔体指数和最小的催化剂残留。 由该催化剂制备的共聚物具有窄的分子量分布,但具有较低的体积密度,低熔体指数和低密度。
    • 6. 发明授权
    • Catalyst composition for polymerizing alpha-olefins and alpha-olefins
polymerization therewith
    • 用于聚合α-烯烃和α-烯烃聚合的催化剂组合物
    • US5096868A
    • 1992-03-17
    • US517952
    • 1990-04-27
    • John T. T. HsiehJeanne C. Simondsen
    • John T. T. HsiehJeanne C. Simondsen
    • C08F4/24C08F10/00C08F210/16
    • C08F10/00C08F210/16
    • A supported catalyst for polymerizing 1-olefins, for example, ethylene, is prepared by depositing a chromium compound and a titanium compound on a refractory oxide support which is substantially non-spherical, and which has a relatively broad particle size distribution range. The catalyst is preferably combined, either outside of the polymerization vessel or in situ, with a sufficient amount of at least one magnesium composition of the formula RMgR', where R and R' are the same or different and they are C.sub.1 to C.sub.12 hydrocarbyl groups, to provide a molar ratio of magnesium to chromium in the catalyst composition of about 0.01:1 to about 25:1. The resulting catalyst composition has good feedability and fluidization characteristics, and it produces resins of relatively high HLMI at relatively low temperatures.There is also disclosed a process for polymerizing 1-olefins, at relatively lower temperatures than was heretofore possible, to obtain resins of relatively high HLMI, using the above-identified catalyst composition. The resulting polymers can be used for the fabrication of blow-molded products, e.g., household and industrial containers.
    • 通过在基本上非球形的耐火氧化物载体上沉积铬化合物和钛化合物并且具有相对宽的粒度分布范围来制备用于聚合1-烯烃,例如乙烯的负载型催化剂。 催化剂优选在聚合容器外部或原位与足量的至少一种式RMgR'的镁组合物组合,其中R和R'相同或不同,并且它们是C1至C12烃基 以提供催化剂组合物中镁与铬的摩尔比为约0.01:1至约25:1。 所得催化剂组合物具有良好的可进给性和流化特性,并且在相对较低的温度下产生相对高的HLMI的树脂。 还公开了使用上述催化剂组合物在相对较低的温度下聚合1-烯烃的方法,以获得相对高的HLMI的树脂。 所得聚合物可用于制造吹塑成型产品,例如家用和工业容器。
    • 9. 发明授权
    • Process for polymerizing a monomer charge
    • 聚合单体电荷的方法
    • US4665140A
    • 1987-05-12
    • US715271
    • 1985-03-25
    • B. Timothy PenningtonPaul V. RolingJohn T. T. Hsieh
    • B. Timothy PenningtonPaul V. RolingJohn T. T. Hsieh
    • C08F4/00C08F2/34C08F4/60C08F4/68C08F10/00C08F10/02
    • C08F10/00Y10S526/901
    • Process of polymerizing a monomer charge including ethylene by (1) drying an inorganic oxide having surface hydroxyl groups to form a support that is substantially free of adsorbed water, (2) reacting the surface hydroxyl groups of the support with at least a substantially stoichiometric amount of at least one organometallic compound corresponding to the formula R.sub.x MR'.sub.y R".sub.z, wherein M is a metal of Group III of the periodic table, R is an alkyl group containing 1 to 12 carbon atoms, R' and R" are independently selected from the group consisting of H, Cl, and alkyl and alkoxy groups containing 1 to 12 carbon atoms, x has a value of 1 to 3, and y and z both represent values of 0 to 2, the sum of which is not greater than 3-x, (3) reacting the thus-treated support with at least about 0.001 mol, per mol of organometallic compound, of at least one vanadium compound corresponding to a formula selected from (RO).sub.n VOX.sub.3-n and (RO).sub.m VX.sub.4-m, in which formulas R represents a C.sub.1 -C.sub.18 monovalent hydrocarbon radical that is free of aliphatic unsaturation, X is Cl or Br, n has a value of 0 to 3, and m has a value of 0 to 4, (4) reacting the product of step 3 with at least about 0.1 mol, per mol of organometallic compound, of an alcohol containing 1 to 18 carbon atoms, (5) feeding the product into a gas-phase reaction zone, (6) feeding a trialkylaluminum into the gas-phase reaction zone in order to form a bed comprising the product and the trialkylaluminum, (7) fluidizing the bed with a gas mixture including ethylene, hydrogen and chloroform, (8) removing particulate polymerized substantially ethylene particles from the reaction zone, and (9) recycling unreacted gas mixture from the top of the reaction zone to the bottom of the reaction zone.
    • 通过(1)干燥具有表面羟基的无机氧化物以形成基本上不含吸附水的载体,聚合包含乙烯的单体电荷的方法,(2)使载体的表面羟基与至少基本上化学计量的量 的至少一种对应于式RxMR'yR''z的有机金属化合物,其中M是周期表第III族金属,R是含有1至12个碳原子的烷基,R'和R“独立地是 选自H,Cl和含有1至12个碳原子的烷基和烷氧基,x具有1至3的值,并且y和z都表示0至2的值,其总和不大于 (3)使如此处理的载体与每摩尔有机金属化合物至少约0.001摩尔至少一种对应于选自(RO)nVOX3-n和(RO)mVX4的式的钒化合物反应 -m,式中R代表C1-C18单价水合 不含脂肪族不饱和键的R 1基团,X为Cl或Br,n为0〜3,m为0〜4,(4)使步骤3的产物与至少约0.1摩尔, 每摩尔有机金属化合物,含有1至18个碳原子的醇,(5)将产物进料到气相反应区,(6)将三烷基铝进料到气相反应区中以形成床, 产物和三烷基铝,(7)用包括乙烯,氢气和氯仿在内的气体混合物使床床流化,(8)从反应区除去颗粒聚合的基本上乙烯的颗粒,和(9)从未反应的气体混合物 反应区到反应区的底部。