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Method of production of middle distillates by hydroisomerization and hydrocracking feeds from the fischer - tropsch process employing a catalyst based on silicon carbide

机译:通过使用基于碳化硅的催化剂的费-托工艺从加氢异构化和加氢裂化进料生产中间馏分的方法

摘要

Preparing middle distillates from a paraffin charge produced by Fischer-Tropsch synthesis comprises implementing a hydrocracking and/or hydroisomerization catalyst comprising at least one hydrodehydrogenating metal comprising metals of group VIB and/or VIII of the periodic table and a composite support formed by a Y-type zeolite and silicon carbide, where the: process is operated at a temperature of 270-400[deg] C, a pressure of 1-9 MPa and hourly volume speed of 0.5-5 hours - 1, and hydrogen flow is adjusted to obtain a ratio of 400-1500 normal liters of hydrogen per liter of charge.
机译:由通过费-托合成法生产的链烷烃进料制备中间馏分包括实施加氢裂化和/或加氢异构化催化剂,该催化剂包括至少一种包含周期表中VIB和/或VIII族金属的加氢脱氢金属和由Y-形成的复合载体。类型的沸石和碳化硅,其中:该方法在270-400℃的温度,1-9 MPa的压力和0.5-5小时的小时体积速度-> 1>下运行,并调节氢气流量以获得每升装料400-1500标准升氢的比例。

著录项

  • 公开/公告号FR2950896B1

    专利类型

  • 公开/公告日2013-01-04

    原文格式PDF

  • 申请/专利权人 IFP;ENI S.P.A.;

    申请/专利号FR20090004771

  • 发明设计人 CHRISTOPHE BOUCHY;

    申请日2009-10-06

  • 分类号C10G65/12;C10G45/64;C10G47/16;B01J29/08;B01J27/224;

  • 国家 FR

  • 入库时间 2022-08-21 16:21:18

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