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    • 3. 发明申请
    • PRODUCTION METHOD OF ALPHA-OLEFIN LOW POLYMER
    • ALPHA-OLEFIN低聚物的生产方法
    • US20090326297A1
    • 2009-12-31
    • US12520096
    • 2007-10-22
    • Hiroki EmotoKei Yoshizuru
    • Hiroki EmotoKei Yoshizuru
    • C07C2/08
    • B01J31/2208B01J31/143B01J2231/12B01J2231/20B01J2531/62C07C2/08C08F10/00Y02P20/52C08F4/69C08F4/22C08F2/06
    • The object of the present invention is to provide a production method of an α-olefin low polymer, wherein a low polymer of an α-olefin is obtained in high yield. The present invention relates to that when an inert gas is allowed to exist in a gas phase part of a reactor 10 in the proportion of from 0.010 to 50.00% by volume, and an α-olefin is subjected to low polymerization reaction in a solvent in the presence of a chromium series catalyst comprising a chromium compound (a), at lest one nitrogen-containing compound (b) selected from the group consisting of an amine, an amide and an imide, and an aluminum-containing compound (c), an unreacted α-olefin and the solvent separated from a reaction liquid are circulated into the reactor 10, and where the proportion of the inert gas in the gas phase exceeds 50.00% by volume, the inert gas is discharged outside the reaction system from a gas phase part of the reactor 10 and/or a circulation piping 21 of an unreacted α-olefin.
    • 本发明的目的是提供一种α-烯烃低聚物的制备方法,其中以高产率获得α-烯烃的低聚物。 本发明涉及当将惰性气体以0.010至50.00%(体积)的比例存在于反应器10的气相部分中,并且在溶剂中使α-烯烃进行低聚合反应时 存在包含铬化合物(a)的铬系催化剂,至少一种选自胺,酰胺和酰亚胺和含铝化合物(c)的含氮化合物(b) 将未反应的α-烯烃和从反应液分离的溶剂循环到反应器10中,并且气相中惰性气体的比例超过50.00体积%时,惰性气体从气体排出到反应体系外 反应器10的相部分和/或未反应的α-烯烃的循环管道21。
    • 6. 发明申请
    • Hindered polyalicyclic alkyl catalysts and their use in a gas-phase polymerization reactor
    • 受阻的多环脂族烷基催化剂及其在气相聚合反应器中的应用
    • US20060128908A1
    • 2006-06-15
    • US11249193
    • 2005-10-13
    • Maria ApecetcheJohn MoorhouseMark GoodeRonald EisingerKevin Cann
    • Maria ApecetcheJohn MoorhouseMark GoodeRonald EisingerKevin Cann
    • C08F2/00
    • C08F10/00C08F10/02C08F110/02C08F210/16C08F4/69C08F4/22C08F2500/12C08F2500/18C08F210/14C08F4/025
    • Embodiments of the present invention include a method of polymerizing olefins comprising contacting olefins with a catalyst composition made by the process of combining a hindered polyalicyclic alkyl catalyst precursor with a particulate inorganic oxide for a deposition time greater than 2 hours to form a catalyst composition. Embodiments of the present invention also include catalyst compositions comprising a hindered polyalicyclic alkyl catalyst precursor made by the process of combining the hindered polyalicyclic alkyl catalyst precursor with a particulate inorganic oxide for a deposition time greater than 2 hours to form the catalyst composition. In one embodiment, the hindered polyalicyclic alkyl catalyst precursor is formed by first combining an acid, a compound having the formula RX, and a metal oxide selected from the group consisting of Group 3 to Group 10 oxide compounds to produce a catalyst precursor; characterized in that R is selected from the group consisting of hindered polyalicyclic alkyls, and substituted derivatives thereof, and X is selected from the group consisting of any suitable leaving group.
    • 本发明的实施方案包括使烯烃聚合的方法,其包括使烯烃与通过将受阻多环脂族烷基催化剂前体与颗粒无机氧化物结合沉积时间大于2小时的方法制备的催化剂组合物形成催化剂组合物。 本发明的实施方案还包括催化剂组合物,其包含通过将受阻多环脂族烷基催化剂前体与颗粒无机氧化物结合沉积时间大于2小时的方法制备的受阻多环脂族烷基催化剂前体,以形成催化剂组合物。 在一个实施方案中,受阻多环脂族烷基催化剂前体通过首先组合酸,具有式RX的化合物和选自第3族至第10族氧化物化合物的金属氧化物以形成催化剂前体而形成; 其特征在于R选自受阻多环脂族烷基及其取代衍生物,X选自任何合适的离去基团。
    • 8. 发明申请
    • Processes for transitioning between chrome-based and mixed polymerization catalysts
    • 铬基和混合聚合催化剂之间过渡的方法
    • US20040214969A1
    • 2004-10-28
    • US10835412
    • 2004-04-29
    • Fred David EhrmanMark Bradley DavisRonald Steven EisingerMark Gregory GoodeMichael Allen Kinnan
    • C08F002/38
    • C08F10/00C08F2/38C08F4/65912C08F4/65925C08F210/16C08F2410/05Y10S526/901C08F4/22C08F2/34C08F2/001C08F2/42C08F210/14C08F2500/18
    • A process of transitioning from a first polymerization reaction conducted in the presence of a mixed catalyst system comprising to a second polymerization reaction conducted in the presence of a chrome-based catalyst system is disclosed, the polymerization reactions being conducted in one embodiment in a polymerization zone of a gas phase fluidized bed reactor which contains a fluidized bed of polymer particles by the essentially continuous passage of monomer gases through the polymerization zone, comprising: a) discontinuing the introduction of the mixed catalyst system into the reactor; b) maintaining polymerization conditions in the reactor and permitting polymerization to continue for a period of time to allow the components of the mixed catalyst system present in the reactor to produce additional polymer particles; c) introducing a deactivating agent into the fluidized bed in an amount sufficient to deactivate the mixed catalyst system; d) establishing optimal conditions within the reactor for the chrome-based catalyst system; and e) introducing the chrome-based catalyst system into the reactor characterized in that the amount of polymer particles in the fluidized bed is substantially maintained in the polymerization zone during the transition steps.
    • 公开了一种从在含铬催化剂体系存在下进行的第二次聚合反应的混合催化剂体系存在下进行的第一聚合反应转变的过程,聚合反应在一个实施方案中在聚合区 的气相流化床反应器,其通过单体气体基本上连续通过聚合区域而包含聚合物颗粒的流化床,包括:a)停止将混合催化剂体系引入反应器; b)保持反应器中的聚合条件并允许聚合持续一段时间,以允许存在于反应器中的混合催化剂体系的组分产生另外的聚合物颗粒; c)以足以使所述混合催化剂体系失活的量将失活剂引入所述​​流化床; d)在铬基催化剂体系的反应器内建立最佳条件; 以及e)将铬基催化剂体系引入反应器,其特征在于在过渡步骤期间,流化床中的聚合物颗粒的量基本上保持在聚合区中。