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    • 1. 发明申请
    • Process to prepare a lubricating base oil and its use
    • 制备润滑油基础油及其用途的工艺
    • US20090159492A1
    • 2009-06-25
    • US11630497
    • 2005-06-23
    • Etienne DuhouxGilbert Robert Bernard GermaineYunus Sajad HusseinJanet Marian SmithersWiecher Derk Evert SteengeDavid John Wedlock
    • Etienne DuhouxGilbert Robert Bernard GermaineYunus Sajad HusseinJanet Marian SmithersWiecher Derk Evert SteengeDavid John Wedlock
    • C10G65/02
    • C10G65/00C10G45/58C10G65/12C10G2400/10
    • Lube base stocks and lube stock compositions, as well as a process for preparing lube base stocks and lube stock compositions, are disclosed. The lube oils preferably have a viscosity index above about 115. The process involves obtaining feed-stocks that have a 95% point below 1150° F. and feedstocks that have 95% point above 1150° F. The feedstocks that have a 95% point below 1150% are catalytically dewaxed, and the feedstocks that have 95% point above 1150% are solvent dewaxed. The resulting products can optionally be blended, and the base stocks can be combined with various additives to form lube oil compositions. Hydrotreatment can optionally be performed on the lube base stocks to remove olefins, oxygenates and other impurities. In one embodiment, one or more of the fractions are obtained from Fisher-Tropsch synthesis. One or more of the fractions can also be obtained from other sources, for example, via distillation of crude oil, provided that the fractions do not include appreciable amounts (i.e., amounts which would adversely affect the catalyst used for catalytic isodewaxing) of thiols or amines. The individual fractions can also includes combinations of feedstocks, from Fisher-Tropsch and other sources.
    • 公开了润滑油基础油和润滑油组合物,以及润滑油基础油和润滑油料组合物的制备方法。 润滑油优选具有高于约115的粘度指数。该方法包括获得在1150°F以下具有95%点的原料,并且具有高于1150°F的95%点的原料。具有95%点的原料 低于1150%的催化脱蜡,并且具有高于1150%的95%点的原料是溶剂脱蜡。 可以任意地混合所得产物,并且可以将基础油料与各种添加剂组合以形成润滑油组合物。 可以任选地在润滑油基础油上进行加氢处理以除去烯烃,含氧化合物和其它杂质。 在一个实施方案中,一种或多种馏分由Fisher-Tropsch合成获得。 一些或多个级分也可以从其他来源获得,例如通过蒸馏原油,条件是馏分不包括可信量(即不利地影响用于催化异构脱蜡的催化剂的量)硫醇或 胺类 单独的馏分还可以包括来自Fisher-Tropsch和其它来源的原料的组合。
    • 3. 发明授权
    • Process to continuously prepare two or more base oil grades and middle distillates
    • 连续制备两种或更多种基础油级和中间馏分的方法
    • US07727379B2
    • 2010-06-01
    • US10591259
    • 2005-03-01
    • Nicholas James AdamsHarmannus Julius HeggeLaurent Georges HuveKevin John Anthony PolderWiecher Derk Evert Steenge
    • Nicholas James AdamsHarmannus Julius HeggeLaurent Georges HuveKevin John Anthony PolderWiecher Derk Evert Steenge
    • C10G65/00C10G69/00
    • C10G65/12C10G45/64
    • Process to prepare simultaneously two or more base oil grades and middle distillates from a mineral crude derived feed, in particular a de-asphalted oil or a vacuum distillate feed or their mixtures, by performing the following steps: (a) hydrocracking the mineral crude derived feed, thereby obtaining an effluent; (b) distillation of the effluent as obtained in step (a) into one or more middle distillates and a full range residue boiling substantially above 340° C., (c) catalytically dewaxing the full range residue by contacting the residue with a dewaxing catalyst comprising a zeolite of the MTW type and a Group VIII metal, thereby obtaining a dewaxed oil; (d) isolating by means of distillation two or more base oil grades from the dewaxed oil obtained in step (c); and (e) isolating a dewaxed gas oil from the dewaxed-oil obtained in step (c); wherein the dewaxed oil as obtained in step (c) comprises between 10 and 40 wt % of a dewaxed heavy gas oil boiling for more than 70 wt % between 370 and 400° C.
    • 通过进行以下步骤同时制备来自矿物原油衍生的原料,特别是脱沥青油或真空馏分进料或其混合物的两种或更多种基础油级和中间馏分的方法:(a)加氢裂化衍生的矿物粗品 进料,从而获得流出物; (b)将步骤(a)中获得的流出物蒸馏成一个或多个中间馏分和基本上沸点高于340℃的全范围残余物,(c)通过使残余物与脱蜡催化剂接触来催化脱蜡全部残余物 包括MTW型沸石和VIII族金属,得到脱蜡油; (d)通过蒸馏从步骤(c)中获得的脱蜡油中分离出两种或更多种基础油级; 和(e)从步骤(c)中获得的脱蜡油中分离脱蜡的瓦斯油; 其中在步骤(c)中获得的脱蜡油包含10-40重量%的在370-400℃之间沸腾超过70重量%的脱蜡重质瓦斯油。