INTEGRATED HYDROCRACKING AND SLURRY HYDROCONVERSION OF HEAVY OILS
    2.
    发明申请
    INTEGRATED HYDROCRACKING AND SLURRY HYDROCONVERSION OF HEAVY OILS 有权
    重油加氢和浆液重油的重油

    公开(公告)号:US20150014217A1

    公开(公告)日:2015-01-15

    申请号:US14308893

    申请日:2014-06-19

    CPC classification number: C10G65/12 C10G45/16 C10G47/26 C10G49/12

    Abstract: Improved yields of fuels and/or lubricants from a resid or other heavy oil feed can be achieved using slurry hydroconversion to convert at least about 90 wt % of the feed. The converted portion of the feed can then be passed into one or more hydroprocessing stages. An initial processing stage can be a hydrotreatment stage for additional removal of contaminants and for passivation of high activity functional groups that may be created during slurry hydroconversion. The hydrotreatment effluent can then be fractionated to separate naphtha boiling range fractions from distillate fuel boiling range fractions and lubricant boiling range fractions. At least the lubricant boiling range fraction can then be hydrocracked to improve the viscosity properties. The hydrocracking effluent can also be dewaxed to improve the cold flow properties. The hydrocracked and/or dewaxed product can then be optionally hydrofinished.

    Abstract translation: 可以使用浆料加氢转化来转化至少约90重量%的进料,从渣油或其他重油进料中提高燃料和/或润滑剂的产率。 然后将进料的转化部分进入一个或多个加氢处理阶段。 初始处理阶段可以是加氢处理阶段,用于额外去除污染物和钝化可能在浆料加氢转化过程中产生的高活性官能团。 然后可以将加氢处理流出物进行分馏,从馏出燃料沸点馏分和润滑剂沸程馏分中分离出石脑油沸程。 至少可以将润滑剂沸程级分进行加氢裂化以提高粘度特性。 加氢裂化流出物也可以脱蜡以改善冷流特性。 加氢裂化和/或脱蜡产物可以任选加氢处理。

    Aromatic alkylation process
    5.
    发明授权
    Aromatic alkylation process 失效
    芳香烷基化工艺

    公开(公告)号:US07019185B2

    公开(公告)日:2006-03-28

    申请号:US10313278

    申请日:2002-12-06

    CPC classification number: C07C2/66 C07C15/085

    Abstract: In a method for producing monoalkylated aromatic compounds, an aromatic feed is contacted with an alkylating agent in the presence of a catalyst comprising a molecular sieve having an X-ray diffraction pattern including d-spacing maxima at 12.4±0.25, 6.9±0.15, 3.57±0.07, and 3.42±0.07 Angstrom. The catalyst also contains at least one metal cation selected from Groups 1–4 and 7–16 of the Periodic Table of Elements, wherein the metal cation is present in an amount of at least 0.5% by weight of the catalyst, whereby selectivity of the catalyst to produce monoalkylates over polyalkylates is improved as compared with the identical catalyst but without the metal cation present.

    Abstract translation: 在制备单烷基化芳族化合物的方法中,芳香族进料在含有分子筛的催化剂存在下与烷基化剂接触,所述催化剂包含具有12.4±0.25,6.9±0.15,3.57的d间距最大值的X射线衍射图 ±0.07和3.42±0.07埃。 催化剂还含有至少一种选自元素周期表第1-4和第7-16部分的金属阳离子,其中金属阳离子的量为催化剂重量的至少0.5%,从而选择性 与相同的催化剂相比,但不存在金属阳离子,催化剂在多烷基化物上产生单烷基化物得到改善。

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