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Catalytic hydrodesulphurisation of heavy residual oils - after sepn. into light and heavy fractions

机译:重质残油的催化加氢脱硫-太阳之后。分为轻重部分

摘要

In the hydrogenating conversion of heavy petroleum residues in a 3-phase fluidised bed of liquid charge, catalyst and H2 at elevated temp. and pressure, the charge is first separated into light and heavy fractions, which are treated separately and the catalyst used for the light fraction is used again for treating the heavy fraction. The process is used for prodn. of high quality fuel oils contg. less sulphur. Consumption of catalyst is reduced by 1.5 times from known processes for treating vacuum residues, and yield of liquid prods. is increased by 2.5 times from that of processes involving previous de-asphalting of the residual oil.
机译:在液相装料,催化剂和氢气的三相流化床中在高温下进行重质石油残留物的氢化转化。在压力和压力下,首先将装料分成轻馏分和重馏分,分别进行处理,然后将用于轻馏分的催化剂再次用于处理重馏分。该过程用于prodn。续续的高质量燃料油更少的硫。与已知的处理真空残留物的方法相比,催化剂的消耗减少了1.5倍,并且液体产物的收率也降低了1.5倍。相对于先前将剩余油脱沥青的工艺而言,其增加了2.5倍。

著录项

  • 公开/公告号FR2396065B1

    专利类型

  • 公开/公告日1980-01-18

    原文格式PDF

  • 申请/专利权人 INSTITUT FRANCAIS DU PETROLE;

    申请/专利号FR19770019874

  • 发明设计人

    申请日1977-06-28

  • 分类号C10G23/08;

  • 国家 FR

  • 入库时间 2022-08-22 17:23:47

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