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    • 3. 发明授权
    • Base oil formulations
    • 基础油配方
    • US08221614B2
    • 2012-07-17
    • US12745930
    • 2008-12-04
    • Gilbert Robert Bernard GermaineDavid John Wedlock
    • Gilbert Robert Bernard GermaineDavid John Wedlock
    • C10M105/04
    • C10M169/04C10M111/04C10M2205/173C10N2220/00C10N2220/022C10N2230/00C10N2230/02C10N2240/08C10N2240/201Y10S208/95
    • Base oil formulation containing (i) a Fischer-Tropsch derived light base oil and (ii) a Fischer-Tropsch derived gas oil. The formulation can be prepared by back-blending a Fischer-Tropsch derived light base oil with a Fischer-Tropsch derived gas oil, for instance derived from the same Fischer-Tropsch synthesis. Also provided is the use of a Fischer-Tropsch derived gas oil in a base oil formulation containing a Fischer-Tropsch derived light base oil, for the purpose of improving the cold flow properties of the formulation while maintaining its flash point above a desired target value, and/or for the purpose of reducing the concentration of a cold flow additive in the formulation, preferably with less of a reduction in the flash point of the formulation than theory would have predicted to occur due to the incorporation of the Fischer-Tropsch derived gas oil.
    • 基础油配方含有(i)费 - 托衍生的轻质基础油和(ii)费 - 托衍生的瓦斯油。 该制剂可以通过将费 - 托衍生的轻质基础油与费 - 托衍生的瓦斯油进行回混来制备,例如衍生自相同的费 - 托合成法。 还提供了在含有费 - 托衍生的轻质基础油的基础油配方中使用费 - 托衍生的瓦斯油,以改进制剂的冷流性质,同时保持其闪点高于所需目标值 ,和/或为了降低制剂中冷流动添加剂的浓度,优选地,与理论预期将由于引入费 - 托衍生物而导致的制剂闪点的降低更少 瓦斯油。
    • 8. 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。