EXTRACTIVE SOLIDS REMOVAL FROM HEAVY FRACTIONS

    公开(公告)号:WO2021201841A1

    公开(公告)日:2021-10-07

    申请号:PCT/US2020/025938

    申请日:2020-03-31

    Abstract: Systems and methods are provided for separation of particles and/or asphaltenes from heavy hydrocarbon fractions. The heavy hydrocarbon fraction can correspond to a feed including particles or a processing effluent that includes particles. If the heavy hydrocarbon fraction is mixed with lower boiling fractions, a separation can be performed to reduce or minimize the amount of hydrocarbons that are present in the heavy hydrocarbon fraction. The heavy hydrocarbon fraction can then be mixed with a sufficient amount of a separation solvent to cause a phase separation. One phase can correspond to the separation solvent plus a portion of the hydrocarbons. The other phase can correspond to hydrocarbons rejected by the separation solvent plus the particles from the heavy hydrocarbon fraction. The phases can then be separated from each other using a solids-liquid centrifugal separator.

    PRODUCTION OF UPGRADED EXTRACT AND RAFFINATE
    2.
    发明申请
    PRODUCTION OF UPGRADED EXTRACT AND RAFFINATE 审中-公开
    升级提取物和RAFFINATE的生产

    公开(公告)号:WO2017205200A1

    公开(公告)日:2017-11-30

    申请号:PCT/US2017/033505

    申请日:2017-05-19

    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).

    Abstract translation: 提供了系统和方法,用于从沸程为400°F(204℃)至1500°F(816℃)的润滑剂沸程进料和/或其它进料生产提质提余液和提取产物。 C)或更多。 升级后的残液和/或提取物产品可具有降低的或最小化的硫,氮,金属或其组合的浓度。 硫,氮和/或金属的浓度降低或最小化可以通过在对应于相对低水平的进料转化的加氢处理条件下加氢处理合适的进料来实现。 任选地,进料也可以脱蜡,例如通过催化脱蜡或通过溶剂脱蜡。 因为不需要过度的芳族饱和度,加氢处理(和任选的脱蜡)的压力可以是500psig(〜3.4MPa)至1200psig(〜8.2MPa)。

    PRODUCTION OF NON-CARCINOGENIC BRIGHTSTOCK EXTRACTS

    公开(公告)号:WO2014158485A3

    公开(公告)日:2014-10-02

    申请号:PCT/US2014/017246

    申请日:2014-02-20

    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.

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