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Multi water-gas shift membrane reactor for the high concentration hydrogen production

机译:用于高浓度制氢的多水煤气变换膜反应器

摘要

The present invention relates to a multi-stage water gas separation membrane reactor for high-efficiency hydrogen production, more particularly by injecting the coal in the dry state, the water, the oxygen as a high concentration of carbon monoxide which is produced through the dry process of the gasification reaction by reacting with the water gas shift catalyst in a single reactor highly purified through the membrane provided in the lower portion and at the same time produces hydrogen and carbon dioxide is a multi-stage water gas separation membrane and for the hydrogen reaction apparatus for separating carbon dioxide. That is, at a temperature of between 1,300-1,500 generated through the partial oxidation and steam gasification reaction of hydrogen, carbon monoxide, carbon dioxide, hydrogen sulfide, carbon monoxide, 50-70% of a low temperature and steam contained in the synthesis gas and the like are a mixture of hydrogen monoxide and to switch to the multi-stage membrane reactor is a high temperature water gas shift catalyst, which is nested in a device discharged to 99.9% of hydrogen and 90% carbon dioxide or more.
机译:用于高效制氢的多级水气分离膜反应器技术领域本发明涉及一种用于高效制氢的多级水气分离膜反应器,更具体地讲,通过以干态注入煤,水,氧气作为通过干法生产的高浓度一氧化碳。在单个反应器中与水煤气变换催化剂反应进行气化反应的过程,该反应器通过下部提供的膜进行高度纯化,同时产生氢气和二氧化碳,是一种多级水煤气分离膜,用于氢气分离二氧化碳的反应装置。即,在通过氢气,一氧化碳,二氧化碳,硫化氢,一氧化碳的部分氧化和蒸汽气化反应产生的1300-1500℃的温度下,低温50-70%和包含在合成气中的蒸汽等是一氧化氢的混合物,并且切换到多级膜反应器是高温水煤气变换催化剂,其嵌套在排放99.9%的氢和90%的二氧化碳或更多的装置中。

著录项

  • 公开/公告号KR101164546B1

    专利类型

  • 公开/公告日2012-07-10

    原文格式PDF

  • 申请/专利权人

    申请/专利号KR20090095166

  • 发明设计人 백일현;김정남;이시훈;

    申请日2009-10-07

  • 分类号C01B3/48;C01B3/38;B01D53/00;

  • 国家 KR

  • 入库时间 2022-08-21 17:07:45

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