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Process and installation for conversion of heavy petroleum fractions in a boiling bed with integrated production of middle distillates with a very low sulphur

机译:沸腾床中重质石油馏分转化的工艺和装置,其中含硫量极低的中间馏分油的综合生产

摘要

Process and installation for conversion of heavy petroleum fractions in a boiling bed with integrated production of middle distillates with a sulphur content of very low.The present invention relates to a process and a plant for the treatment of a supply of heavy oil, of which at least 80% by weight have a boiling point greater than 340 198 C, with which the process comprises the following stages: (a) in a reactor hidroconversu00e3o The boiling bed operating with a high flow rate of liquid and gas.Conversion in% by weight of a fraction having a boiling point greater than 540198 C and from 10 to 98% by weight; (b) the separation of the effluent obtained from stage (a) in a gas containing hydrogen and H ~ 2 ~ s.A fraction comprising diesel oil and optionally a fraction that is heavier than the fraction of diesel and a naphtha hydrotreating; (c) through contact with at least a catalyst of at least a fraction comprising the gas obtained in the stage (b); (d) separation of Eph. Luente obtained at the end of the stage (c) in a gas containing hydrogen and at least one fraction of diesel fuel having a contentSulphur content of less than 50 ppm, preferably less than 20 ppm and more preferably less than 10 ppm, the stage of hidroconversu00e3o (a) being conducted in a pressure P1 and the stage of T (c) being conducted in a pressure P2, the difference 30 P = P1 - P2. As for me In the 3 MPa.The supply of hydrogen to the stages of hidroconversu00e3o (H) and (c) being ensured by a compression system only with N stages.
机译:重沸馏分在沸腾床中转化的方法和装置,其中硫含量非常低的中间馏分油的综合生产。本发明涉及一种用于处理重油供应的方法和设备,其中至少80%(重量)的沸点高于340 <198> C,该过程包括以下步骤:(a)在反应器中沸腾床以高的液体和气体流速运行。沸点大于540198> C且10至98重量%的馏分的重量百分比; (b)在含氢​​和H〜2〜s的气体中分离从步骤(a)得到的流出物。馏分包括柴油和可选的重于柴油和石脑油加氢精制的馏分; (c)通过与至少一部分包含在步骤(b)中获得的气体的至少一种催化剂接触; (d)弗的分离。在步骤(c)结束时在含氢和至少一部分柴油中的硫含量小于50 ppm,优选小于20 ppm,更优选小于10 ppm的气体中获得的朗特高压转换(a)在压力P1下进行,而T(c)阶段在压力P2下进行,差值<30> P = P1-P2。对于我而言,在3 MPa压力下,仅通过N级压缩系统可确保向hidroconvers (H)和(c)级提供氢气。

著录项

  • 公开/公告号BRPI0700654A

    专利类型

  • 公开/公告日2007-11-06

    原文格式PDF

  • 申请/专利权人 IFP;

    申请/专利号BR2007PI00654

  • 申请日2007-03-08

  • 分类号C10G65/12;

  • 国家 BR

  • 入库时间 2022-08-21 20:59:15

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