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Process and apparatus for the conversion of heavy hydrocarbon oils into lighter oils

机译:将重质烃油转化为轻油的方法和设备

摘要

275,120. Northrup, V. W. March 21. 1927. Mineral oils. - In a process for converting heavier hydrocarbon oils into lighter hydrocarbon oils, a mixture of the vapours of the heavier hydrocarbons and gas having available hydrogen is passed through an electrified zone and thereafter through a catalyzing zone independent of the electrifying zone. Heavier hydrocarbon vapours from a vaporizer A are passed up a tube B to which hydrogen, methane, natural gas, &c. is admitted at C1. An insulated wire D is suspended within the tube B and a source of high tension alternating current is connected between the wire D and the tube, the potential difference being from 2000 to 8000 volts according to the type of heavy petroleum employed. From the tube B, the electrified mixture passes to a catalyzing chamber comprising converters consisting of lagged and heated tubes I in which are supported corrugated tubes J; the tubes I, J are composed of, or coated with catalytic material, for example, nickel, cobalt, palladium, aluminium, iron, or mixtures thereof, for example, nickel containing 5 per cent of iron and 5 per cent aluminium. The temperature of the catalyzing chamber depends upon the type of heavy petroleum used and may be from about 725‹ to about 1000‹ F., the temperature of the various converters within the catalyzing chamber being successively slightly higher. From the catalyzing chamber, the mixture passes to a dephlegmating tower M, and thence to a cooler O maintained at about 200‹ F. to 400‹ F., whereby heavier vapours are condensed, the light product passing in vapour form to a condenser Q1.
机译:275,120。 Northrup,V. W.,1927年3月21日。矿物油。 -在将重质烃油转化为轻质烃油的方法中,将重质烃的蒸气和具有可用氢的气体的混合物通过带电区,然后通过独立于带电区的催化区。来自汽化器A的较重的烃类蒸气通过管B流通,氢,甲烷,天然气等气体进入管B。在C 1被接纳。绝缘电线D悬挂在管子B内,并且高压交流电源连接在电线D和管子之间,根据所用重石油的类型,电势差为2000至8000伏。带电的混合物从管B进入催化室,该催化室包括转化器,该转化器由滞后的加热管I组成,并在其中支撑着波纹管J;管I,J由例如镍,钴,钯,铝,铁或它们的混合物的催化材料组成或涂覆有催化材料,例如含5%铁和5%铝的镍。催化室的温度取决于所使用的重质石油的类型,并且可以为约725°F至约1000°F。催化室内的各种转化器的温度依次略高。混合物从催化室进入分馏塔M,然后进入保持在约200°F至400°F的冷却器O,从而使较重的蒸汽冷凝,轻质产物以蒸汽形式进入冷凝器Q。 <1>。

著录项

  • 公开/公告号GB275120A

    专利类型

  • 公开/公告日1927-08-04

    原文格式PDF

  • 申请/专利权人 VERNON WILLIAM NORTHRUP;

    申请/专利号GB19270007742

  • 发明设计人

    申请日1927-03-21

  • 分类号C10G15/00;

  • 国家 GB

  • 入库时间 2022-08-24 10:13:46

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