公开(公告)号：US11680214B2

公开(公告)日：2023-06-20

申请号：US17277646

申请日：2019-08-28

申请人： SHELL OIL COMPANY

发明人： Nariman Boumendjel ,  Ralf Gunnar Meister ,  Cornelis Hyacinthus Maria Van Der Hulst ,  Nicolaas Van Dijk

IPC分类号： C10G65/12 ,  C10M101/02 ,  C10N20/00 ,  C10N30/00 ,  C10N20/02

CPC分类号： C10G65/12 ,  C10M101/02 ,  C10G2300/1074 ,  C10G2300/202 ,  C10G2300/205 ,  C10G2300/206 ,  C10G2300/301 ,  C10G2300/302 ,  C10G2300/304 ,  C10G2300/308 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/70 ,  C10G2400/10 ,  C10M2203/1006 ,  C10N2020/011 ,  C10N2020/02 ,  C10N2030/43

摘要： A process for producing a base oil composition from a deasphalted oil (DAO) feed, where the DAO feed undergoes hydrotreating, hydrocracking, catalytically dewaxing, hydrofinishing, and fractionating to generate the base oil composition. The base oil composition includes a hazy-free at 0° C. heavy base oil comprising (a) a kinetic viscosity ranging from 15 to 21 cSt at 100° C., (b) a 5 viscosity index of at least 95, (c) a pour point of less than −12° C., (d) a cloud point of less than −18° C., and (e) a total aromatics content of 2 wt % or less, where the hazy-free at 0° C. heavy base oil maintains a hazy-free appearance when stored undisturbed at 0° C. during a test period.

公开(公告)号：US10590361B2

公开(公告)日：2020-03-17

申请号：US14652224

申请日：2013-12-17

申请人： SHELL OIL COMPANY

发明人： John Joseph Baric ,  Nicolaas Van Dijk ,  Laurent Georges Huve

IPC分类号： C10G65/12 ,  C10M101/02 ,  C10G73/44 ,  C10G47/16 ,  B01J29/076 ,  B01J23/882 ,  B01J29/16

摘要： The invention provides a process for preparing a hydrowax comprising the steps of: (a) providing a hydrocarbonaceous feedstock which contains more than 4% by weight of hydrocarbons boiling in the range of from 550 to 800° C.; (b) hydrotreating the hydrocarbonaceous feedstock with a hydrotreating catalyst in the presence of a hydrogen-containing gas under hydrotreating conditions to obtain a hydrotreated product; (c) hydrocracking at least part of the hydrotreated product as obtained in step (b) with a hydrocracking catalyst in the presence of a hydrogen-containing gas under hydrocracking conditions to obtain a hydrocracked product, which hydrocracking catalyst contains a zeolitic component which is present in an amount of at least 14 wt %, based on the total weight of the hydrocracking catalyst, and wherein the volume ratio of the hydrotreating catalyst as used in step (b) and the hydrocracking catalyst is more than 1; and (d) recovering from the hydrocracked product as obtained in step (c) the hydrowax.