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    • 2. 发明申请
    • Method of hydrotreating gas oil fraction
    • 加氢处理瓦斯油馏分的方法
    • US20060211900A1
    • 2006-09-21
    • US10548313
    • 2004-03-05
    • Hideshi IkiYukihiro SugiuraYuichi TanakaShinya Takahashi
    • Hideshi IkiYukihiro SugiuraYuichi TanakaShinya Takahashi
    • C07C1/00
    • B01J23/85B01J23/883B01J35/1019B01J35/1038B01J35/1061B01J37/20C10G2400/06
    • The gas oil fraction hydrotreatment process of the invention is characterized by using a gas oil fraction with a sulfur content of 0.8-2% by mass and a total aromatic content of 20-35% by volume as the feed oil and subjecting the feed oil to hydrotreatment in the presence of a hydrogenation catalyst comprising at least one metal from among Group 6A metals and at least one metal from among Group 8 metals as active metals, and under reaction conditions with a reaction temperature of 330-390° C., a hydrogen partial pressure of 12-20 MPa and a liquid hourly space velocity of 0.1-1 h−1, to obtain an ultralow sulfur and low- aromatic gas oil fraction having a sulfur content of not greater than 1 ppm by mass and a total aromatic content of not greater than 1% by volume. This hydrotreatment process allows production of a “zero sulfur” and “zero aromatic” gas oil fraction in an efficient and reliable manner without provision of special operating conditions or equipment investment.
    • 本发明的粗柴油馏分加氢处理方法的特征在于,使用硫含量为0.8〜2质量%,总芳烃含量为20〜35体积%的粗柴油馏分作为原料油, 在包含至少一种金属的6A族金属和至少一种金属作为活性金属的第8族金属中进行加氢处理,在反应温度为330-390℃的反应条件下,加氢处理 12-20MPa的分压和0.1-1小时-1的液时空速,得到硫含量不大于1ppm的超低硫和低芳烃瓦斯油馏分 并且总芳族含量不大于1体积%。 该加氢处理方法允许以有效和可靠的方式生产“零硫”和“零芳烃”瓦斯油馏分,而不需要特殊的操作条件或设备投资。