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    PROCESS TO PRODUCE POLYALPHAOLEFINS
    5.
    发明申请
    PROCESS TO PRODUCE POLYALPHAOLEFINS 审中-公开
    生产聚烯烃的方法

    公开(公告)号：WO2009017953A3

    公开(公告)日：2009-04-16

    申请号：PCT/US2008069832

    申请日：2008-07-11

    Applicant: EXXONMOBIL CHEMICAL PATENT INC ,  WU MARGARET MAY-SOM ,  HAGEMEISTER MARK ,  YANG NORMAN

    Inventor： WU MARGARET MAY-SOM ,  HAGEMEISTER MARK ,  YANG NORMAN

    IPC: C08F10/00 ,  C08F4/6592

    CPC classification number: C08F10/00 ,  C08F110/14 ,  Y02P20/582 ,  C08F4/65912 ,  C08F4/65927 ,  C08F4/65908 ,  C08F2500/03 ,  C08F2500/17

    Abstract: Liquid poly-alpha-olefins are obtained by a) contacting in a reaction zone, alpha- olefin monomers with a non-coordinating anion activator, a single bridged meso-metallocene transition metal compound, and a co-activator, and ethylene is not present at more than 30 volume % of the monomers entering the reaction zone, and the alpha-olefm 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 no more than 5% monomer is converted from olefin to alkane. The liquid polyalphaolefin product has a pour point of less than 25°C, a KV1oo of 2 to 6000 cSt, 20 weight percent dimer or less and a viscosity index of 60 or more.

    Abstract translation: 液体聚-α-烯烃通过以下方式获得：a）在反应区中使α-烯烃单体与非配位阴离子活化剂，单桥接的内消旋金属茂过渡金属化合物和共活化剂接触，并且乙烯不存在 在超过30体积％的进入反应区的单体中，并且基于内消旋 - 茂金属，非配位阴离子活化剂的重量，进料组分中的α-烯烃单体以至少20重量％或更多的量存在， 共活化剂，单体和溶剂或稀释剂，并且其中不超过5％的单体从烯烃转化为烷烃。 液体聚α-烯烃产品的倾点低于25℃，KV100为2至6000cSt，20重量％二聚体或更低，粘度指数为60或更高。

    PROCESS TO PRODUCE POLYALPHAOLEFINS
    6.
    发明申请
    PROCESS TO PRODUCE POLYALPHAOLEFINS 审中-公开
    生产聚合物的方法

    公开(公告)号：WO2009017953A2

    公开(公告)日：2009-02-05

    申请号：PCT/US2008/069832

    申请日：2008-07-11

    Applicant: EXXONMOBIL CHEMICAL PATENT INC. ,  WU, Margaret, May-Som ,  HAGEMEISTER, Mark ,  YANG, Norman

    Inventor： WU, Margaret, May-Som ,  HAGEMEISTER, Mark ,  YANG, Norman

    IPC: C08F10/00 ,  C08F4/6592

    CPC classification number: C08F10/00 ,  C08F110/14 ,  Y02P20/582 ,  C08F4/65912 ,  C08F4/65927 ,  C08F4/65908 ,  C08F2500/03 ,  C08F2500/17

    Abstract: Liquid poly-alpha-olefins are obtained by a) contacting in a reaction zone, alpha- olefin monomers with a non-coordinating anion activator, a single bridged meso-metallocene transition metal compound, and a co-activator, and ethylene is not present at more than 30 volume % of the monomers entering the reaction zone, and the alpha-olefm 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 no more than 5% monomer is converted from olefin to alkane. The liquid polyalphaolefin product has a pour point of less than 25°C, a KV1oo of 2 to 6000 cSt, 20 weight percent dimer or less and a viscosity index of 60 or more.

    Abstract translation: 液体聚-α-烯烃通过以下方法获得：a）在反应区中接触α-烯烃单体与非配位阴离子活化剂，单桥式内消旋 - 金属茂过渡金属化合物和共活化剂，并且不存在乙烯 以超过30体积％的进入反应区的单体，并且进料组分中的α-烯烃单体以基于中金属茂，非配位阴离子活化剂的重量计至少为20重量％或更多， 共活化剂，单体和溶剂或稀释剂，并且其中不超过5％的单体从烯烃转化为烷烃。 液体聚α-烯烃产物的倾点低于25℃，KV1oo为2至6000cSt，20重量％二聚物或更低，粘度指数为60或更大。

    POLYOLEFINS FROM NON-CONVENTIONAL FEEDS
    8.
    发明申请
    POLYOLEFINS FROM NON-CONVENTIONAL FEEDS 审中-公开
    非常规饲料的多糖

    公开(公告)号：WO2007064392A1

    公开(公告)日：2007-06-07

    申请号：PCT/US2006/038069

    申请日：2006-09-28

    Applicant: EXXONMOBIL CHEMICAL PATENTS INC. ,  WU, Margaret, May-Som ,  KRAMER, Anatoly, I. ,  YANG, Norman

    Inventor： WU, Margaret, May-Som ,  KRAMER, Anatoly, I. ,  YANG, Norman

    IPC: C10G69/12 ,  C10M107/02

    CPC classification number: C10M107/10 ,  C10G69/126 ,  C10M2205/0285 ,  C10N2230/08

    Abstract: Polyolefins made in accordance with the present invention are produced by polymerizing an unsaturated olefin or combination of unsaturated olefins to produce an unsaturated polyolefin, isomerizing the unsaturated polyolefin in the presence of an acid catalyst under conditions to produce a substantially unsaturated-isomerized polyolefin, and hydrogenating the unsaturated-isomerized polyolefin to produce a saturated isomerized polyolefin. A lube oil comprising the inventive saturated isomerized polyolefin is also disclosed.

    Abstract translation: 根据本发明制备的聚烯烃通过使不饱和烯烃或不饱和烯烃的组合聚合以制备不饱和聚烯烃，在酸催化剂存在下，在产生基本上不饱和异构化的聚烯烃的条件下异构化不饱和聚烯烃，并氢化 不饱和异构化的聚烯烃以产生饱和异构化的聚烯烃。 还公开了包含本发明的饱和异构化聚烯烃的润滑油。

    PROCESS TO PRODUCE POLYALPHAOLEFINS
    10.
    发明申请
    PROCESS TO PRODUCE POLYALPHAOLEFINS 审中-公开
    生产聚合物的方法

    公开(公告)号：WO2009017953A8

    公开(公告)日：2010-04-01

    申请号：PCT/US2008069832

    申请日：2008-07-11

    Applicant: EXXONMOBIL CHEM PATENTS INC ,  WU MARGARET MAY-SOM ,  HAGEMEISTER MARK ,  YANG NORMAN

    Inventor： WU MARGARET MAY-SOM ,  HAGEMEISTER MARK ,  YANG NORMAN

    IPC: C08F10/00 ,  C08F4/6592

    CPC classification number: C08F10/00 ,  C08F110/14 ,  Y02P20/582 ,  C08F4/65912 ,  C08F4/65927 ,  C08F4/65908 ,  C08F2500/03 ,  C08F2500/17

    Abstract: Liquid poly-alpha-olefins are obtained by a) contacting in a reaction zone, alpha- olefin monomers with a non-coordinating anion activator, a single bridged meso-metallocene transition metal compound, and a co-activator, and ethylene is not present at more than 30 volume % of the monomers entering the reaction zone, and the alpha-olefm 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 no more than 5% monomer is converted from olefin to alkane. The liquid polyalphaolefin product has a pour point of less than 25°C, a KV1oo of 2 to 6000 cSt, 20 weight percent dimer or less and a viscosity index of 60 or more.

    Abstract translation: 液体聚-α-烯烃通过以下方法获得：a）在反应区中接触α-烯烃单体与非配位阴离子活化剂，单桥式内消旋 - 金属茂过渡金属化合物和共活化剂，并且不存在乙烯 以超过30体积％的进入反应区的单体，并且进料组分中的α-烯烃单体以基于中金属茂，非配位阴离子活化剂的重量计至少为20重量％或更多， 共活化剂，单体和溶剂或稀释剂，并且其中不超过5％的单体从烯烃转化为烷烃。 液体聚α-烯烃产物的倾点小于25℃，KV1oo为2至6000cSt，20重量％二聚物或更低，粘度指数为60或更大。

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