PRODUCTION OF LUBRICANT OILS FROM THERMALLY CRACKED RESIDS
    4.
    发明申请
    PRODUCTION OF LUBRICANT OILS FROM THERMALLY CRACKED RESIDS 审中-公开
    从热破碎的树脂生产润滑油

    公开(公告)号:US20160298048A1

    公开(公告)日:2016-10-13

    申请号:US15096867

    申请日:2016-04-12

    Abstract: Methods are provided for processing deasphalted gas oils derived from thermally cracked resid fractions to form Group I, Group II, and/or Group III lubricant base oils. The yield of lubricant base oils (optionally also referred to as base stocks) can be increased by thermally cracking a resid fraction at an intermediate level of single pass severity relative to conventional methods. By performing thermal cracking to a partial level of conversion, compounds within a resid fraction that are beneficial for increasing both the viscosity and the viscosity index of a lubricant base oil can be retained, thus allowing for an improved yield of higher viscosity lubricant base oils from a thermally cracked resid fraction.

    Abstract translation: 提供了用于处理衍生自热裂化残渣馏分的脱沥青瓦斯油以形成组I,组II和/或组III润滑剂基础油的方法。 相对于常规方法,润滑剂基础油(任选地也称为基础油料)的产率可以通过以单程严重程度的中间水平热裂解渣油馏分来提高。 通过对部分转化水平进行热裂解,可以保留残渣部分中有利于提高润滑剂基础油的粘度和粘度指数的化合物,从而可以提高较高粘度的润滑剂基础油的产率, 热裂解渣油馏分。

    Production of non-carcinogenic brightstock extracts
    5.
    发明授权
    Production of non-carcinogenic brightstock extracts 有权
    生产不致癌的亮片提取物

    公开(公告)号:US08986537B2

    公开(公告)日:2015-03-24

    申请号:US13803454

    申请日:2013-03-14

    Abstract: Provided are multiple correlations for relationships between MI value for a brightstock extract and the distillation cut point temperature used for separation of the vacuum resid that is used to form the brightstock extract. Based on these correlations, a BSE having a desired MI value can be formed based on an adjustment of the distillation cut point temperature. A first correlation establishes a relationship between a fractional weight boiling temperature for a vacuum resid fraction and a distillation cut point temperature for separating the vacuum resid fraction from at least one distillate fraction in a feedstock. A second correlation establishes a relationship between a fractional weight boiling temperature for a brightstock extract derived from the vacuum resid fraction, and the fractional weight boiling temperature for the vacuum resid fraction. A third correlation has been established between the fractional weight boiling temperature for the brightstock extract and a mutagenicity index value.

    Abstract translation: 对于明矾提取物的MI值与用于分离用于形成亮片提取物的真空渣油的蒸馏切割点温度之间的关系,提供多重相关性。 基于这些相关性,可以基于蒸馏切割点温度的调节形成具有期望MI值的BSE。 第一相关性建立了真空残渣馏分的分数重量沸点温度与用于将减压渣油馏分与原料中的至少一个馏出物馏分分离的蒸馏切割点温度之间的关系。 第二相关性确定了来自真空残渣馏分的亮片提取物的分数重量沸点温度与减压渣油馏分的分数重量沸点温度之间的关系。 在亮片提取物的分数重量沸点温度和致突变性指数值之间已经建立了第三个相关性。

    PRODUCTION OF NON-CARCINOGENIC BRIGHTSTOCK EXTRACTS
    6.
    发明申请
    PRODUCTION OF NON-CARCINOGENIC BRIGHTSTOCK EXTRACTS 有权
    生产非致癌性亮点提取物

    公开(公告)号:US20140262958A1

    公开(公告)日:2014-09-18

    申请号:US13803454

    申请日:2013-03-14

    Abstract: Provided are multiple correlations for relationships between MI value for a brightstock extract and the distillation cut point temperature used for separation of the vacuum resid that is used to form the brightstock extract. Based on these correlations, a BSE having a desired MI value can be formed based on an adjustment of the distillation cut point temperature. A first correlation establishes a relationship between a fractional weight boiling temperature for a vacuum resid fraction and a distillation cut point temperature for separating the vacuum resid fraction from at least one distillate fraction in a feedstock. A second correlation establishes a relationship between a fractional weight boiling temperature for a brightstock extract derived from the vacuum resid fraction, and the fractional weight boiling temperature for the vacuum resid fraction. A third correlation has been established between the fractional weight boiling temperature for the brightstock extract and a mutagenicity index value.

    Abstract translation: 对于明矾提取物的MI值与用于分离用于形成亮片提取物的真空渣油的蒸馏切割点温度之间的关系,提供多重相关性。 基于这些相关性,可以基于蒸馏切割点温度的调节形成具有期望MI值的BSE。 第一相关性建立了真空残渣馏分的分数重量沸点温度与用于将减压渣油馏分与原料中的至少一个馏出物馏分分离的蒸馏切割点温度之间的关系。 第二相关性确定了来自真空残渣馏分的亮片提取物的分数重量沸点温度与减压渣油馏分的分数重量沸点温度之间的关系。 在亮片提取物的分数重量沸点温度和致突变性指数值之间已经建立了第三个相关性。

    Forming asphalt fractions from three-product deasphalting

    公开(公告)号:US10655077B2

    公开(公告)日:2020-05-19

    申请号:US16031288

    申请日:2018-07-10

    Abstract: Systems and methods are provided for using a three-product deasphalter to produce advantageous combinations of deasphalted oil, resin, and rock. The desaphalted oil, resin, and rock can then be further combined, optionally with other vacuum gas oil fractions produced during the distillation that generated the feed to the three-product deasphalter, to produce a product slate of improved quality while also maintaining the quality of the resulting asphalt product and reducing or minimizing the amount of lower value products generated. The additional “resin” product from the three product deasphalter can be generated by sequential deasphalting, by using a resin settler to separate resin from the deasphalted oil, or by any other convenient method.

    PRODUCTION OF UPGRADED EXTRACT AND RAFFINATE

    公开(公告)号:US20200002625A1

    公开(公告)日:2020-01-02

    申请号:US16567218

    申请日:2019-09-11

    Abstract: Systems and methods are provided for producing upgraded raffinate and extract products from lubricant boiling range feeds and/or other feeds having a boiling range of 400° F. (204° C.) to 1500° F. (816° C.) or more. The upgraded raffinate and/or extract products can have a reduced or minimized concentration of sulfur, nitrogen, metals, or a combination thereof. The reduced or minimized concentration of sulfur, nitrogen, and/or metals can be achieved by hydrotreating a suitable feed under hydrotreatment conditions corresponding to relatively low levels of feed conversion. Optionally, the feed can also dewaxed, such as by catalytic dewaxing or by solvent dewaxing. Because excessive aromatic saturation is not desired, the pressure for hydrotreatment (and optional dewaxing) can be 500 psig (˜3.4 MPa) to 1200 psig (˜8.2 MPa).

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