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Selectively permeable membrane reactor and hydrogen production method using a selectively permeable membrane reactor

机译:选择性渗透膜反应器和使用选择性渗透膜反应器的制氢方法

摘要

In the hydrogen production process of the present invention, A [ml / min], the amount of hydrogen that has not passed through the selectively permeable membrane (non-permeated hydrogen amount of hydrogen separated by passing through the permselective membrane (permeated hydrogen amount) when as B [ml / min] amount), the value of the hydrogen recovery is defined by the following equation becomes a 60~99%, (CO 2), one the partial pressure of carbon dioxide at the outlet of the reaction tube When the (CO) and the partial pressure of carbon oxides, and to K the equilibrium constant for the disproportionation of carbon monoxide in the reaction tube temperature, under the condition that the value defined by the following equation α is 0.6 or more I do the production of hydrogen. Hydrogen recovery rate = 100 × {A / (A + B)} α ={(CO 2) / (CO) 2} / K
机译:在本发明的制氢方法中,A [ml / min]是未通过选择性渗透膜的氢的量(通过渗透选择性膜分离出的氢的非渗透氢量(渗透氢量))当以B [ml / min]的量计时,氢气回收率的值由下式定义为<60%〜99%,(CO 2),其中二氧化碳的分压为在以下方程式α定义的条件下,当碳氧化物的(CO)和分压为K时,反应管温度下一氧化碳歧化的平衡常数为K时的反应常数。我做0.6以上的氢的生产。氢回收率= 100×{A /(A + B)}α = {(CO 2)/(CO)2} / K

著录项

  • 公开/公告号JPWO2007108543A1

    专利类型

  • 公开/公告日2009-08-06

    原文格式PDF

  • 申请/专利权人 日本碍子株式会社;

    申请/专利号JP20080506350

  • 发明设计人 森 伸彦;中村 俊之;

    申请日2007-03-23

  • 分类号C01B3/32;C01B3/56;

  • 国家 JP

  • 入库时间 2022-08-21 19:38:32

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