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    • 5. 发明申请
    • Process To Produce Polyalphaolefins
    • 生产聚α-烯烃的方法
    • US20090036725A1
    • 2009-02-05
    • US11832287
    • 2007-08-01
    • Margaret M. WuMark P. HagemeisterNorman Yang
    • Margaret M. WuMark P. HagemeisterNorman Yang
    • C07C2/02
    • C08F10/00C08F110/14Y02P20/582C08F4/65912C08F4/65927C08F4/65908C08F2500/03C08F2500/17
    • The present invention relates to processes to produce liquid poly-alpha-olefins comprising: a) contacting in a reaction zone, in the presence of from 0 to 60 psi hydrogen, one or more C3 to C20 alpha-olefin monomers with a non-coordinating anion activator, a single bridged meso-metallocene transition metal compound having less than about 35 wt % racemic isomer, and a co-activator selected from the group consisting of alkyl aluminum compounds and alkyl alumoxanes, provided that when the alkyl alumoxane is present it is present in a molar ratio of less than 0.1:1 of alkylalumoxane to meso-metallocene, and provided that when the alkyl aluminum compound is present it is present at a molar ratio of alkyl aluminum to meso-metallocene of from 2:1 to 10,000 to 1, where the molar ratio of activator to meso-metallocene is from 10:1 to 0.1:1, and provided that ethylene is not present at more than 30 volume % of the monomers entering the reaction zone, and provided that the alpha-olefin monomers in the feed components are present in at least 20 wt % or more based upon the weight of the meso-metallocene, non-coordinating anion activator, co-activator, monomers, and solvent or diluent, and where: i) the productivity of the process is at least 50,000 g of total product per gram of transition metal compound (where the total product is defined to be the total amount of product exiting the reactor, minus unreacted monomers and solvents); and ii) no more than 5% monomer is converted from olefin to alkane; and b) obtaining a liquid polyalphaolefin product having a pour point of less than 25° C., a KV100 of 2 to 6000 cSt, 20 weight percent dimer or less and a viscosity index of 60 or more.
    • 本发明涉及制备液体聚-α-烯烃的方法,包括:a)在0至60psi氢气存在下,在反应区中使一个或多个C 3至C 20α-烯烃单体与非配位的 阴离子活化剂,具有小于约35重量%外消旋异构体的单桥连的内消旋 - 金属茂过渡金属化合物,以及选自烷基铝化合物和烷基铝氧烷的共活化剂,条件是当烷基铝氧烷存在时,它是 以烷基铝氧烷与内消旋金属茂的摩尔比小于0.1:1存在,并且当烷基铝化合物存在时,其烷基铝与内消旋金属茂的摩尔比为2:1至10,000至 1,其中活化剂与内消旋金属茂的摩尔比为10:1至0.1:1,并且条件是进入反应区的单体的体积百分比不超过30体积%,并且条件是α-烯烃 单体i 基于内消旋金属茂,非配位阴离子活化剂,共活化剂,单体和溶剂或稀释剂的重量,进料组分以至少20重量%或更多的重量存在,其中:i) 每克过渡金属化合物的总产物至少为50,000g(其中总产物定义为离开反应器的产物的总量,减去未反应的单体和溶剂); 和ii)不超过5%的单体从烯烃转化为烷烃; 和b)获得倾点小于25℃,KV100为2至6000cSt,20重量%二聚物或更低,粘度指数为60以上的液体聚α-烯烃产物。
    • 6. 发明授权
    • Process to produce polyalphaolefins
    • 生产聚α-烯烃的方法
    • US08513478B2
    • 2013-08-20
    • US11832287
    • 2007-08-01
    • Margaret M. WuMark P. HagemeisterNorman Yang
    • Margaret M. WuMark P. HagemeisterNorman Yang
    • C07C2/22
    • C08F10/00C08F110/14Y02P20/582C08F4/65912C08F4/65927C08F4/65908C08F2500/03C08F2500/17
    • Liquid poly-alpha-olefins having a KV100 of 2 to 6000 cSt, 20 weight percent dimer or less and a viscosity index of 60 or more are obtained by contacting in a reaction zone, in the presence of from 0 to 60 psi hydrogen, C3 to C20 alpha-olefin monomers with a non-coordinating anion activator, a single bridged meso-metallocene transition metal compound having less than about 35 wt % racemic isomer, and a co-activator. The molar ratio of activator to meso-metallocene is from 10:1 to 0.1:1, and the alpha-olefin monomers in the feed components are present in at least 20 wt % or more based upon the weight of the meso-metallocene, non-coordinating anion activator, co-activator, monomers, and solvent or diluent. The productivity of the process is at least 50,000 g of total product per gram of transition metal compound and no more than 5% monomer is converted from olefin to alkane.
    • 通过在0至60psi的氢气,C3的存在下在反应区中接触,获得KV100为2至6000cSt,20重量%的二聚物或更低的粘度指数为60或更大的液体聚α-烯烃, 具有非配位阴离子活化剂的C 20α-烯烃单体,具有小于约35重量%外消旋异构体的单桥连内消旋金属茂过渡金属化合物和共活化剂。 活化剂与内消旋金属茂的摩尔比为10:1至0.1:1,并且进料组分中的α-烯烃单体以基于内消旋金属茂的重量计至少为20重量%或更多, 配位阴离子活化剂,共活化剂,单体和溶剂或稀释剂。 该方法的生产率为每克过渡金属化合物至少50,000g总产物,并且不超过5%的单体由烯烃转化为烷烃。
    • 7. 发明授权
    • Catalyst recovery process
    • 催化剂回收过程
    • US07652185B2
    • 2010-01-26
    • US10565143
    • 2004-08-17
    • Norman YangShakeel Tirmizi
    • Norman YangShakeel Tirmizi
    • C07C2/02C07C7/00
    • B01J38/68B01J27/32C07C2/20C07C7/04C07C2527/1213Y02P20/584Y10S585/904C07C11/02
    • A process for reducing boron trifluoride usage and emissions associated with PAO manufacture, the process comprising distilling a portion of the crude PAO product containing a boron trifluoride-organic catalyst at a temperature sufficient to cause the boron trifluoride-organic catalyst to dissociate to produce an overhead stream comprising uncomplexed boron trifluoride and an uncomplexed organic catalyst component, contacting the uncomplexed boron trifluoride and uncomplexed organic catalyst component in a condenser column having an internal structure that increases the recombination of the uncomplexed boron trifluoride and uncomplexed organic catalyst component to form a recycle boron trifluoride-organic catalyst.
    • 一种减少与三氯化硼生产相关的三氟化硼使用和排放的方法,该方法包括在足以引起三氟化硼 - 有机催化剂解离以产生塔顶馏出物的温度下蒸馏含有三氟化硼 - 有机催化剂的一部分粗制PAO产物 包含未络合的三氟化硼和未络合的有机催化剂组分的流,在具有增加未络合的三氟化硼和未络合的有机催化剂组分的复合的内部结构的冷凝器塔中使未络合的三氟化硼和未络合的有机催化剂组分接触以形成再循环三氟化硼 无机催化剂。
    • 10. 发明申请
    • Catalyst recovery process
    • 催化剂回收过程
    • US20060178545A1
    • 2006-08-10
    • US10565143
    • 2004-08-17
    • Norman YangShakeel Tirmizi
    • Norman YangShakeel Tirmizi
    • C07C2/02
    • B01J38/68B01J27/32C07C2/20C07C7/04C07C2527/1213Y02P20/584Y10S585/904C07C11/02
    • A process for reducing boron trifluoride usage and emissions associated with PAO manufacture, the process comprising distilling a portion of the crude PAO product containing a boron trifluoride-organic catalyst at a temperature sufficient to cause the boron trifluoride-organic catalyst to dissociate to produce an overhead stream comprising uncomplexed boron trifluoride and an uncomplexed organic catalyst component, contacting the uncomplexed boron trifluoride and uncomplexed organic catalyst component in a condenser column having an internal structure that increases the recombination of the uncomplexed boron trifluoride and uncomplexed organic catalyst component to form a recycle boron trifluoride-organic catalyst.
    • 一种减少与三氯化硼生产相关的三氟化硼使用和排放的方法,该方法包括在足以引起三氟化硼 - 有机催化剂解离以产生塔顶馏出物的温度下蒸馏含有三氟化硼 - 有机催化剂的一部分粗制PAO产物 包含未络合的三氟化硼和未络合的有机催化剂组分的流,在具有增加未络合的三氟化硼和未络合的有机催化剂组分的复合的内部结构的冷凝器塔中使未络合的三氟化硼和未络合的有机催化剂组分接触以形成再循环三氟化硼 无机催化剂。