Catalyst system for dewaxing
    2.
    发明授权

    公开(公告)号:US11351528B2

    公开(公告)日:2022-06-07

    申请号:US17047987

    申请日:2019-04-05

    申请人: SHELL OIL COMPANY

    摘要: A catalyst system for dewaxing of a hydrocarbon feedstock comprising a mixture of a first dewaxing catalyst composition and a second dewaxing catalyst composition, wherein the first dewaxing catalyst composition is a ZSM-12 zeolite based catalyst composition and the second dewaxing catalyst composition is a EU-2 and/or ZSM-48 zeolite based catalyst composition, and wherein a concentration gradient of the mixture is achieved within a single catalyst bed, such that the concentration of the first dewaxing catalyst is decreasing and the concentration of the second dewaxing catalyst is increasing through the catalyst bed; and a process for dewaxing of a hydrocarbon feedstock comprising contacting the hydrocarbon feedstock with said catalyst system.

    PROCESS TO PREPARE MIDDLE DISTILLATES AND BASE OILS
    6.
    发明申请
    PROCESS TO PREPARE MIDDLE DISTILLATES AND BASE OILS 审中-公开
    制备中间馏分和基础油的方法

    公开(公告)号:US20150184089A1

    公开(公告)日:2015-07-02

    申请号:US14408607

    申请日:2013-06-28

    申请人: SHELL OIL COMPANY

    IPC分类号: C10G69/00

    摘要: A process to prepare a first middle distillates fraction, a second middle distillates fraction, a distillate base oil and a residual base oil by providing a Fischer-Tropsch product stream; separating the Fischer-Tropsch product stream to obtain at least a low boiling fraction, boiling below a temperature ranging from 300 to 450° C., and a high boiling fraction, boiling above a temperature ranging from 300 to 450° C.; subjecting the high boiling fraction to a hydrocracking/hydroisomerization step to obtain a partially isomerised product stream; separating the partially isomerised product stream to obtain a first middle distillates fraction, a heavy distillates fraction and a residual fraction, the residual fraction having a T5 wt. % boiling point between 400 and 650° C.; dewaxing the low boiling fraction to obtain a second middle distillates fraction; dewaxing the heavy distillates fraction to obtain a distillate base oil; and dewaxing the residual fraction to obtain a residual base oil.

    摘要翻译: 通过提供费 - 托产物流来制备第一中间馏分,第二中间馏分,馏出物基油和残余基础油的方法; 分离费 - 托产物流以获得沸点低于300-450℃的沸点,沸点高于300-450℃的高沸点馏分。 将高沸点馏分进行加氢裂化/加氢异构化步骤以获得部分异构化的产物流; 分离部分异构化的产物流以获得第一中间馏分馏分,重馏分馏分和残余馏分,残余馏分具有T5wt。 沸点在400和650℃之间。 将低沸点馏分脱蜡以获得第二中间馏分; 将重馏分馏分脱蜡,得到馏出物基油; 并将残余馏分脱蜡以获得残留的基础油。

    Process for preparing a diesel fuel composition

    公开(公告)号:US11084997B2

    公开(公告)日:2021-08-10

    申请号:US15774191

    申请日:2016-11-10

    申请人: SHELL OIL COMPANY

    IPC分类号: C10L1/08

    摘要: Process for preparing a diesel fuel composition comprising the steps of: (i) blending a Fischer-Tropsch derived gasoil with a petroleum derived gasoil to form a blended gasoil which is compliant with the EN590 specification, wherein the Fischer-Tropsch derived gasoil has a density of 0.8 g/cm3 or less and wherein the petroleum derived gasoil is derived from naphthenic high density petroleum crude oil and has a density at 15° C. of 0.84 g/cm3 or greater and a naphthenics content of 30 wt % or greater; and (ii) mixing the blended gasoil produced in step (i) with a diesel base fuel to form a diesel fuel composition, wherein the diesel fuel composition has a density at 15° C. in the range from 0.820 g/cm3 to 0.845 g/cm3.

    PROCESS TO PREPARE MIDDLE DISTILLATES AND BASE OILS
    10.
    发明申请
    PROCESS TO PREPARE MIDDLE DISTILLATES AND BASE OILS 审中-公开
    制备中间馏分和基础油的方法

    公开(公告)号:US20150203769A1

    公开(公告)日:2015-07-23

    申请号:US14408579

    申请日:2013-06-28

    申请人: SHELL OIL COMPANY

    IPC分类号: C10G67/02 C10G73/44

    摘要: A process to prepare a first middle distillates fraction, a second middle distillates fraction and one or more base oils, the process comprising the steps of providing a Fischer-Tropsch product stream; separating the Fischer-Tropsch product stream to obtain at least a low boiling fraction, boiling below a temperature in the range of from 300 to 450° C., and a high boiling fraction, boiling above a temperature in the range of from 300 to 450° C.; subjecting the high boiling fraction to a hydrocracking/hydroisomerization step to obtain an at least partially isomerised product stream; separating the partially isomerised product stream to obtain a first middle distillates fraction and a residual fraction, wherein the residual fraction has a T10 wt. % boiling point of between 200 and 450° C.; dewaxing the low boiling fraction to obtain a second middle distillates fraction; and dewaxing the residual fraction to obtain one or more base oils.

    摘要翻译: 一种制备第一中间馏分馏分,第二中间馏分和一种或多种基础油的方法,该方法包括提供费 - 托产物流的步骤; 分离费 - 托产物流以获得至少一个沸点低于300-450℃的沸点,沸点高于300-450℃的高沸点馏分 C。; 将高沸点馏分进行加氢裂化/加氢异构化步骤以获得至少部分异构化的产物流; 分离部分异构化的产物流以获得第一中间馏分馏分和残余馏分,其中残余馏分具有T10wt。 沸点百分比在200-450℃之间。 将低沸点馏分脱蜡以获得第二中间馏分; 并将残余馏分脱蜡以获得一种或多种基础油。