首页> 外国专利> Improvements in the production of hydrogen, carbon monoxide/hydrogen mixtures of nitrogen/hydrogen mixtures

Improvements in the production of hydrogen, carbon monoxide/hydrogen mixtures of nitrogen/hydrogen mixtures

机译:改进氢气,一氧化碳/氢气混合物和氮气/氢气混合物的生产

摘要

In the production of hydrogen, alone or mixed with carbon monoxide or nitrogen, partial combustion of gaseous hydrocarbons or gases containing the same is effected with such an amount of oxygen or air that no deposition of carbon occurs during combustion and the gaseous products are passed over solid carbonaceous matter, e.g. coke, at a high temperature, e.g. 1200 DEG C., the heat generated in the combustion stage being such that no blowing period is required to maintain the temperature of the coke. Steam may be added either before or after the primary combustion stage. When dealing with a gas mixture containing 60 per cent of methane, not less than 40 per cent of oxygen must be supplied; more oxygen, however, is preferably employed, e.g. equal volumes of the two gases. In the case of ethane, more than one volume of oxygen to one of ethane is used, preferably up to two volumes of oxygen to one of ethane. In practice, a coke bed is provided at one end of the combustion chamber and oxygen, or air, and the hydrocarbon gas are separately preheated, the p temperature of the hydrocarbon gas being such that carbon is not deposited. In the case of methane, 900 DEG C. should not be exceeded, and the preheater should be constructed from materials inimical to the production of carbon, e.g. austenitic alloy steels or silica. The oxygen or air may be heated to as high a temperature as possible. The final gas mixture may be catalyzed with steam to convert the carbon monoxide to dioxide which is removed, leaving a mixture of nitrogen and hydrogen. If pure hydrogen be required, the monoxide and nitrogen may be removed by low temperature treatment. Steam used in the process may be obtained from the heat of the gases after the preheating stage, or by spraying water into the hot gases after leaving the coke bed. An example dealing with methane is furnished and Specifications 29367/10, [Class 55 (i), Coking &c.], and 247,176, [Class 90, Non-metallic elements], are referred to.
机译:在单独或与一氧化碳或氮混合的氢气生产中,气态碳氢化合物或含碳氢化合物的气体的部分燃烧是通过一定量的氧气或空气进行的,以致在燃烧过程中不会发生碳沉积,并且气态产物会通过固体碳质物质,例如高温下的焦炭在1200℃下,在燃烧阶段产生的热量使得不需要吹气周期来保持焦炭的温度。可以在一级燃烧阶段之前或之后添加蒸汽。当处理含60%甲烷的混合气体时,必须提供不少于40%的氧气。然而,优选使用更多的氧,例如。等体积的两种气体。在乙烷的情况下,相对于一种乙烷使用多于一体积的氧气,对于一种乙烷优选使用多于二体积的氧气。实际上,在燃烧室的一端设有焦炭床,氧气或空气被分别预热,碳氢化合物气体的p温度使得碳不沉积。在甲烷的情况下,不应超过900℃,并且预热器应由对碳的生产不利的材料制成,例如碳。奥氏体合金钢或二氧化硅。氧气或空气可以加热到尽可能高的温度。最终的气体混合物可以用蒸汽催化,以将一氧化碳转化为二氧化碳,将其除去,剩下氮气和氢气的混合物。如果需要纯氢,则可以通过低温处理除去一氧化氮和氮。该过程中使用的蒸汽可以从预热阶段之后的气体热量中获得,也可以从离开焦炭床后的热气体中喷水。提供了处理甲烷的示例,并参考了规格29367/10([焦炭等,类别55(i))和247,176,[类别90,非金属元素]。

著录项

  • 公开/公告号GB349471A

    专利类型

  • 公开/公告日1931-05-26

    原文格式PDF

  • 申请/专利号GB19300006381

  • 发明设计人

    申请日1930-02-26

  • 分类号C01B3/02;C01B3/36;C01B3/48;

  • 国家 GB

  • 入库时间 2022-08-24 08:20:51

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号