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    Process for manufacturing lubricating base oil with high monocycloparaffins and low multicycloparaffins
    2.
    发明申请
    Process for manufacturing lubricating base oil with high monocycloparaffins and low multicycloparaffins 有权
    制造具有高单环烷烃和低多环烷烃的润滑油基油的方法

    公开(公告)号：US20050133409A1

    公开(公告)日：2005-06-23

    申请号：US10744870

    申请日：2003-12-23

    申请人： Susan Abernathy ,  David Kramer ,  John Rosenbaum ,  Stephen Miller ,  Russell Krug

    发明人： Susan Abernathy ,  David Kramer ,  John Rosenbaum ,  Stephen Miller ,  Russell Krug

    IPC分类号： C10G45/64 ,  C10G73/38

    CPC分类号： C10G45/64 ,  C10G2400/10 ,  Y10S208/95

    摘要： A process for manufacturing a lubricating base oil by: a) performing Fischer-Tropsch synthesis on syngas to provide a product stream; b) isolating from said product stream a substantially paraffinic wax feed having less than about 30 ppm total nitrogen and sulfur, and less than about 1 wt % oxygen; c) dewaxing said feed by hydroisomerization dewaxing using a shape selective intermediate pore size molecular sieve comprising a noble metal hydrogenation component, wherein the hydroisomerization temperature is between about 600° F. (315° C.) and about 750° F. (399° C.), to produce an is dimerized oil; and d) hydrofinishing said isomerized oil to produce a lubricating base oil having specific desired properties.

    摘要翻译： 一种制造润滑油基础油的方法，该方法是：a）在合成气上进行费 - 托合成以提供产物流; b）从所述产物流中分离具有小于约30ppm总氮和硫以及小于约1重量％氧的基本上石蜡的蜡进料; c）使用包含贵金属氢化组分的形状选择性中孔分子筛通过加氢异构化脱蜡来脱蜡所述进料，其中加氢异构化温度在约600°F（315℃）至约750°F（399° C.），以产生二聚油; 和d）加氢精制所述异构化油以产生具有特定所需性能的润滑基础油。

    Process for making lubricating base oils with high ratio of monocycloparaffins to multicycloparaffins
    5.
    发明申请
    Process for making lubricating base oils with high ratio of monocycloparaffins to multicycloparaffins 失效
    制造具有高比例的单环烷烃的润滑基础油与多环烷烃的方法

    公开(公告)号：US20060289337A1

    公开(公告)日：2006-12-28

    申请号：US11438108

    申请日：2006-05-19

    申请人： John Rosenbaum ,  Nancy Bertrand ,  Scott Deskin ,  Kamala Krishna ,  Stephen Miller ,  Susan Abernathy

    发明人： John Rosenbaum ,  Nancy Bertrand ,  Scott Deskin ,  Kamala Krishna ,  Stephen Miller ,  Susan Abernathy

    IPC分类号： C10G73/02

    CPC分类号： C10G45/64 ,  C10G2/32 ,  C10G65/043 ,  C10G2400/10 ,  Y10S208/95

    摘要： A process for manufacturing a lubricating base oil, comprising dewaxing a substantially paraffinic wax feed by hydroisomerization dewaxing using a shape selective intermediate pore size molecular sieve under hydroisomerization conditions including a hydrogen to feed ratio from about 712.4 to about 3562 liter H2/liter oil, whereby a lubricating base oil is produced having a)a total weight percent of molecules with cycloparaffinic functionality greater than 10, and b) a ratio of weight percent molecules with monocycloparaffinic functionality to weight percent molecules with multicycloparaffinic functionality greater than 30. Also a method for producing a base oil having a high ratio of weight percent molecules with monocycloparaffinic functionality to weight percent molecules with multicycloparaffinic functionality by hydroisomerization dewaxing a selected Fischer-Tropsch wax under hydroisomerization conditions including a hydrogen to feed ratio from about 712.4 to about 3562 liter H2/liter oil. Also a lubricating base oil manufacturing plant.

    摘要翻译： 一种润滑油基础油的制造方法，其特征在于，在加氢异构化条件下，通过使用形状选择性中等孔径分子筛，通过加氢异构化脱蜡将大体上链烷烃化的蜡进料脱蜡，所述加氢异构化条件包括氢与进料比约为712.4〜3562升H 2， / l油，由此产生润滑基础油，其具有a）具有大于10的环烷烃官能团的分子的总重量百分比，以及b）分子与单环烷烃官能团的重量百分比与重均分子百分比的多环烷烃官能团的比例更大 30.另外，通过在加氢异构化条件下加氢异构化脱蜡选择的费 - 托蜡来生产具有高单体重量百分比的分子与单环烷属官能度的重量百分比的基础油的方法，其中多烷基官能度分子的重量百分比为约712.4 至约3562 升H 2 /升/升油。 也是润滑油基础油生产厂。

    Process to make white oil from waxy feed using highly selective and active wax hydroisomerization catalyst
    7.
    发明申请
    Process to make white oil from waxy feed using highly selective and active wax hydroisomerization catalyst 有权
    使用高选择性和活性蜡加氢异构化催化剂从蜡质进料制备白油的方法

    公开(公告)号：US20060016724A1

    公开(公告)日：2006-01-26

    申请号：US10897906

    申请日：2004-07-22

    申请人： Stephen Miller ,  Susan Abernathy ,  John Rosenbaum

    发明人： Stephen Miller ,  Susan Abernathy ,  John Rosenbaum

    IPC分类号： C10G73/38

    CPC分类号： C10G45/64 ,  C10G2400/14

    摘要： A process for producing one or more white oils, by: a) hydroisomerization dewaxing a waxy feed with a defined composition over a highly selective and active wax hydroisomerization catalyst with a defined composition under conditions sufficient to produce a white oil; and b) collecting one or more white oils, wherein the yield of white oils is high, and they have a low pour point and a good Saybolt color. Also, a process for producing medicinal grade white oils, by a)hydroisomerization dewaxing a waxy feed with a defined composition over a highly selective and active wax hydroisomerization catalyst with a defined composition under conditions sufficient to produce a white oil, b) collecting technical grade white oils having a low pour point and good Saybolt color in high yield, and c) hydrofinishing the technical grade white oils at conditions sufficient to produce medicinal grade white oils that pass the RCS test.

    摘要翻译： 一种生产一种或多种白油的方法，通过以下步骤：a）在足够产生白色油的条件下，以具有规定组成的高选择性和活性蜡加氢异构化催化剂加氢异构化将具有规定组成的蜡质进料脱蜡; 和b）收集一种或多种白油，其中白油的产率高，并且它们具有低倾点和良好的Saybolt颜色。 另外，生产医药级白油的方法是通过以下方式进行加氢异构化：以足够产生白色油的条件，在具有规定组成的高选择性和活性蜡加氢异构化催化剂上，以具有规定组成的蜡质进料脱蜡，b）收集技术等级 具有低倾点和良好Saybolt颜色的白色油以高产率，以及c）在足以产生通过RCS试验的药用级白油的条件下加氢精制技术级白色油。

    White oil from waxy feed using highly selective and active wax hydroisomerization catalyst
    9.
    发明申请
    White oil from waxy feed using highly selective and active wax hydroisomerization catalyst 有权
    使用高选择性和活性蜡加氢异构化催化剂的来自蜡质进料的白油

    公开(公告)号：US20060016721A1

    公开(公告)日：2006-01-26

    申请号：US10897501

    申请日：2004-07-22

    申请人： Stephen Miller ,  Susan Abernathy ,  John Rosenbaum

    发明人： Stephen Miller ,  Susan Abernathy ,  John Rosenbaum

    IPC分类号： H01B3/22

    CPC分类号： C10M107/02 ,  C10G2300/30 ,  C10G2300/302 ,  C10G2300/304 ,  C10G2400/14 ,  C10M2205/173 ,  C10N2220/022 ,  C10N2220/13 ,  C10N2230/20 ,  C10N2230/40 ,  C10N2230/43 ,  C10N2230/62

    摘要： A composition of white oil having a kinematic viscosity at 100° C. between about 1.5 cSt and 36 cSt, a viscosity index greater than an amount calculated by the equation: Viscosity Index=28×Ln(the Kinematic Viscosity at 100° C.)+105, less than 18 weight percent of molecules with cycloparaffin functionality, a pour point less than zero degrees C., and a Saybolt color of +20 or greater. Also, a composition of white oil having a kinematic viscosity at 100° C. between about 1.5 cSt and 36 cSt, a viscosity index greater than an amount calculated by the equation: Viscosity Index=28×Ln(the Kinematic Viscosity at 100° C.)+95, between 5 and less than 18 weight percent of molecules with cycloparaffin functionality, less than 1.2 weight percent molecules with multicycloparaffin functionality, a pour point less than zero degrees C., and a Saybolt color of +20 or greater.

    摘要翻译： 在100℃下运动粘度在约1.5cSt和36cSt之间的粘度指数大于由下式计算的量的白油组合物：粘度指数= 28xLn（100℃下的运动粘度）+ 105 ，小于18重量％的具有环烷烃官能团的分子，倾点小于零摄氏度，Saybolt颜色为+20或更大。 另外，在100℃下的运动粘度在约1.5cSt和36cSt之间的粘度指数大于由下式计算的量的白油组合物：粘度指数= 28×Ln（100℃下的运动粘度） +95，小于18重量％的具有环烷烃官能团的分子，小于1.2重量％的具有多环烷烃官能团的分子，倾点小于零摄氏度，Saybolt颜色为+20或更大。