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    Process for making lubricating base oils with high ratio of monocycloparaffins to multicycloparaffins
    2.
    发明授权
    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：US07763161B2

    公开(公告)日：2010-07-27

    申请号：US11438108

    申请日：2006-05-19

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

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

    IPC分类号： C10G45/00 ,  C10M105/02

    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： 一种润滑基础油的制造方法，其特征在于，在加氢异构化条件下，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-约3562升H 2 /升油， 制备润滑基础油，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度的重量百分比与重均分子百分比的重量百分比的比例，多环烷烃官能度大于30.而且， 通过在加氢异构化条件下加氢异构化脱蜡所选的费 - 托蜡，将具有单环烷属官能团的重量百分比的重量百分比的分子与多环烷属官能团的重量百分比高的基础油，包括氢与进料比为约712.4至约3562升H 2 / 迭油。 也是润滑油基础油生产厂。

    PROCESS TO MAKE A 110 NEUTRAL BASE OIL WITH IMPROVED PROPERTIES
    10.
    发明申请
    PROCESS TO MAKE A 110 NEUTRAL BASE OIL WITH IMPROVED PROPERTIES 审中-公开
    制备具有改进性能的110中性基础油的方法

    公开(公告)号：US20100078353A1

    公开(公告)日：2010-04-01

    申请号：US12481862

    申请日：2009-06-10

    申请人： John M. Rosenbaum ,  Brent K. Lok ,  Kathy A. Helling ,  Ryan J. Schexnaydre ,  Scott C. Deskin ,  Susan M. Abernathy

    发明人： John M. Rosenbaum ,  Brent K. Lok ,  Kathy A. Helling ,  Ryan J. Schexnaydre ,  Scott C. Deskin ,  Susan M. Abernathy

    IPC分类号： C10L1/04 ,  C10G7/00

    CPC分类号： G01N33/26 ,  G01N11/00

    摘要： A process to manufacture a base oil, comprising selecting an original base oil having an original VI, an original volatility, and an original CCS VIS; and removing a lower boiling fraction, whereby the base oil is made having a kinematic viscosity at 100° C. from 4.2 to 4.6 mm2/s, a VI that is at least 4 higher than the original VI, a volatility that is at least 3 wt % lower than the original volatility, and a CCS VIS that is within 200 mPa·s of the original CCS VIS. A process to manufacture a base oil, comprising selecting an original base oil and removing a lower boiling fraction from the original base oil, whereby the base oil has a ratio of a Noack Volatility to a CCS VIS at −25° C. multiplied by 100 from 0.80 to 1.55. Also a base oil, made by the processes disclosed herein.

    摘要翻译： 一种制造基础油的方法，包括选择原始VI原始挥发性原始基础油和原始CCS VIS; 并除去低沸点馏分，由此使基油在100℃下的运动粘度为4.2至4.6mm 2 / s，比原始VI高至少4的VI，至少为3的挥发度 比原始挥发性低的wt％，CCS VIS在原始CCS VIS的200 mPa·s以内。 一种制造基础油的方法，包括选择原始基础油并从原始基础油中除去低沸点馏分，由此基础油在-25℃下的Noack挥发度与CCS VIS的比率乘以100 从0.80到1.55。 也是由本文公开的方法制成的基础油。