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    A process for the production of low-sulfur diesel gas oil
    3.
    发明公开
    A process for the production of low-sulfur diesel gas oil 失效
    Verfahren zur Erzeugung von Diesel-Gasölmit niedrigem Schwefelgehalt。

    公开(公告)号：EP0523679A2

    公开(公告)日：1993-01-20

    申请号：EP92112111.7

    申请日：1992-07-15

    申请人： NIPPON OIL CO., LTD. ,  NIPPON PETROLEUM REFINING CO., LTD

    发明人： Ushio, Masaru, c/o Nippon Oil Co., Ltd. ,  Nakano, Tamio, c/o Nippon Oil Co., Ltd. ,  Hatayama, Minoru, c/o Nippon Oil Co., Ltd. ,  Ishikawa, Katuhiko, c/o Nippon Oil Co., Ltd. ,  Sato, Masaru, c/o Nippon Oil Co., Ltd.

    IPC分类号： C10G65/04

    CPC分类号： C10G65/04 ,  C10G2400/04 ,  F02B3/06

    摘要： A process for the production of a low-sulfur diesel gas oil having a sulfur content of 0.05 % by weight or lower and having a Saybolt color number of -10 or higher, from a petroleum distillate having a sulfur content of 0.1 to 2.0 % by weight and having an inferior color and inferior oxidation stability.
    The process comprises contacting the petroleum distillate with hydrogen in the presence of a hydro-treating catalyst which has at least one metal and a porous carrier, wherin said metal has a hydro-treating activity and is supported on said porous carrier, at a temperature of 350 to 450 °C, and a pressure of 45 to 100 kg/cm² in the first step to thereby produce materials having a sulfur content of 0.05 % by weight or lower, and contacting further the materials issued from the first step with hydrogen in the presence of a hydro-treating catalyst which has at least one metal and a porous carrier, wherin said metal has a hydro-treating activity and is supported on said porous carrier, at a temperature of 200 to 300 °C, and a pressure of 45 to 100 kg/cm² in the second step to thereby produce the finished low-sulfur diesel gas oil.

    摘要翻译： 从硫含量为0.1〜2.0％的石油馏分中生产硫含量为0.05重量％以下且Saybolt色数为-10以上的低硫柴油瓦斯油的方法， 重量较差，氧化稳定性差。 该方法包括在具有至少一种金属和多孔载体的加氢处理催化剂的存在下使石油馏出物与氢接触，所述金属具有加氢处理活性，并且在所述多孔载体上负载在所述多孔载体上， 350〜450℃，第一工序中的压力为45〜100kg / cm 2，由此制造硫含量为0.05重量％以下的材料，并使第一步骤发出的材料与 在具有至少一种金属和多孔载体的氢化处理催化剂的存在下，在所述多孔载体上，在所述多孔载体上，在200〜300℃的温度下，加入氢， 在第二步骤中压力为45至100kg / cm 2，从而生产完成的低硫柴油瓦斯油。