首页> 外国专利> Process for treating a temperature-sensitive hydrocarbonaceous stream containing a non-distillable component to produce a hydrogenated distillable hydrocarbonaceous product

Process for treating a temperature-sensitive hydrocarbonaceous stream containing a non-distillable component to produce a hydrogenated distillable hydrocarbonaceous product

机译:处理含有不可蒸馏组分的热敏烃物流以生产氢化可蒸馏烃产物的方法

摘要

A process for treating a temperature-sensitive hydrocarbonaceous stream containing a non-distillable component to produce a hydrogenated distillable hydrocarbonaceous product and a heavy product comprising the non-distillable component while minimizing thermal degradation of the hydrocarbonaceous stream which process comprises the steps of: (a) contacting the hydrocarbonaceous stream with a first hydrogen-rich gaseous stream having a temperature greater than the hydrocarbonaceous stream in a flash zone at flash conditions thereby increasing the temperature of the hydrocarbonaceous stream with minimal thermal degradation and vaporizing at least a portion thereof to provide a hydrocarbonaceous vapor stream comprising hydrogen and a heavy product comprising the non-distillable component; (b) contacting the hydrocarbonaceous vapor stream comprising hydrogen recovered from step (a) without intermediate separation with a hydrogenation catalyst in a hydrogenation reaction zone at hydrogenation conditions to increase the hydrogen content of the hydrocarbonaceous compounds contained in the hydrocarbonaceous vapor stream; (c) condensing at least a portion of the resulting effluent from the hydrogenation reaction zone to provide a second hydrogen-rich gaseous stream and a liquid stream comprising hydrogenated distillable hydrocarbonaceous compounds; and (d) recovering a hydrogenated distillable hydrocarbonaceous product from the liquid stream comprising hydrogenated distillable hydrocarbonaceous compounds.
机译:一种处理含有不可蒸馏组分的热敏烃物流以生产氢化可蒸馏烃产物和包含该不可蒸馏组分的重产物的方法,同时使烃物流的热降解减至最小,该方法包括以下步骤: )在闪蒸条件下,使含烃物流与温度高于闪蒸区中含烃物流的第一富氢气态物流接触,从而以最小的热降解提高含烃物流的温度,并蒸发至少一部分以提供含氢的烃蒸气流和含不可蒸馏组分的重产物; (b)在氢化条件下,在氢化条件下,将不经中间分离而将从步骤(a)中回收的氢的含烃蒸气流与氢化催化剂接触,以增加含烃蒸气流中含烃化合物的氢含量; (c)冷凝至少一部分来自氢化反应区的所得流出物,以提供第二富氢气态物流和包含氢化可蒸馏烃类化合物的液态物流; (d)从包含氢化可蒸馏烃类化合物的液流中回收氢化可蒸馏烃类产物。

著录项

  • 公开/公告号US4923590A

    专利类型

  • 公开/公告日1990-05-08

    原文格式PDF

  • 申请/专利权人 UOP;

    申请/专利号US19890302518

  • 发明设计人 ROBERT B. JAMES JR.;TOM N. KALNES;

    申请日1989-01-27

  • 分类号C10G65/04;

  • 国家 US

  • 入库时间 2022-08-22 06:07:32

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