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Hydrocarbon conversion process utilizing a magnetic field in a fluidized bed of catalytic particles

机译:利用磁场在催化颗粒流化床中的烃转化工艺

摘要

A hydrocarbon conversion process, such as catalytic desulfurization of a vaporized petroleum feedstock with hydrogen or catalytic reforming of a vaporized hydrocarbon feedstock, is carried out by passing the gaseous medium upwardly through a fluidized bed of magnetizable composite particles having catalytic activity for hydrocarbon conversion and which contain 2 to 40 volume % ferro- or ferrimagnetic material . .to.!. .Iadd. in .Iaddend.a nontime varying (direct current) and substantially uniform applied magnetic field having a substantial component along the direction of gravity such that the composite particles have a component of magnetization along the direction of gravity. The gaseous medium is also the fluidizing medium passing upwardly at a superficial gas velocity ranging between:PP (1) at least twice the normal minimum superficial gas velocity required to fluidize the bed in the absence of said applied magnetic field, and PP (2) less than the superficial gas velocity required to cause time-varying fluctuations of pressure difference through said bed for a 0.1 to 1 second time interval during continuous fluidization in the presence of said applied magnetic field.
机译:通过使气态介质向上通过具有催化活性以进行烃转化的可磁化复合颗粒的流化床,进行烃转化工艺,例如用氢对气化的石油原料进行催化脱硫或对气化的烃原料进行催化重整。包含2至40体积%的铁磁性或亚铁磁性材料。 。至。!。 。我加。此外,在非时间变化的(直流电)和基本上均匀的施加的磁场中,沿重力方向具有相当大的分量,使得复合颗粒沿重力方向具有磁化分量。气态介质也是流态化介质,其表观气体速度在以下范围内向上流动:(P)

(1)至少是在没有所述施加磁场的情况下流化床所需的正常最小表观气体速度的两倍, (2)小于在存在所述施加磁场的情况下在连续流化过程中在0.1至1秒的时间间隔内引起通过所述床的压力差的时变波动所需的表观气体速度。

著录项

  • 公开/公告号USRE31186E

    专利类型

  • 公开/公告日1983-03-22

    原文格式PDF

  • 申请/专利权人

    申请/专利号US19800221372

  • 发明设计人 RONALD E. ROSENSWEIG;

    申请日1980-12-30

  • 分类号C10G23/10;C10G35/14;

  • 国家 US

  • 入库时间 2022-08-22 09:48:02

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