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Method of production of middle distillates by hydroisomerization and hydrocracking of a heavy fraction coming from the effluent produced by the process fischer - tropsch

机译:通过加氢异构化和加氢裂化费托托工艺产生的废水产生的重馏分生产中间馏分的方法。

摘要

The invention concerns a process and apparatus wherein the paraffin effluent from the Fischer-Tropsch process is separated into a heavy fraction with an initial boiling point of 120-200° C., said heavy fraction then optionally being hydrotreated then brought into contact with an amorphous hydroisomerization/hydrocracking catalyst that converts at least 80% by weight of the 370° C.+ products into products with a boiling point of less than 370° C. After distilling the hydrocracked fraction obtained to separate middle distillates, the residual heavy fraction is recycled.
机译:本发明涉及一种方法和设备,其中将来自费-托工艺的石蜡流出物分离成初始沸点为120-200℃的重馏分,然后将所述重馏分任选地加氢处理然后使其与无定形物接触。加氢异构化/加氢裂化催化剂,将至少80%(重量)的370°C +产物转化为沸点低于370°C的产物。蒸馏所得加氢裂化馏分以分离中间馏出物后,将剩余的重质馏分回收。

著录项

  • 公开/公告号FR2826972B1

    专利类型

  • 公开/公告日2007-03-23

    原文格式PDF

  • 申请/专利权人 INSTITUT FRANCAIS DU PETROLE;

    申请/专利号FR20010008970

  • 发明设计人 ERIC BENAZZI;CHRISTOPHE GUERET;

    申请日2001-07-06

  • 分类号C10G65/12;

  • 国家 FR

  • 入库时间 2022-08-21 20:27:14

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