β=a/bwherein a denotes the volume of the reforming catalyst layer [cm3], and b denotes the area of the permselective membrane [cm2]."/> Process for producing hydrogen with permselective membrane reactor and permselective membrane reactor
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Process for producing hydrogen with permselective membrane reactor and permselective membrane reactor

机译:选择性渗透膜反应器和选择性渗透膜反应器生产氢气的方法

摘要

A permselective membrane reactor is provided, including a reactor tube having a gas inlet at one end and a gas outlet at the other end thereof. A separator tube is disposed in the reactor tube and has a permselective membrane selectively permeable to hydrogen on a surface thereof and a discharge outlet for passing separated gas through the permselective membrane. The permselective membrane reactor also includes a layer comprising a reforming catalyst that promotes reforming of ethanol, so that β, defined by the following equation, is in a range of 0.05 to 20:β=a/bwherein a denotes the volume of the reforming catalyst layer [cm3], and b denotes the area of the permselective membrane [cm2].
机译:提供了一种选择性渗透膜反应器,包括反应器管,该反应器管的一端具有进气口,另一端具有出气口。分离管设置在反应器管中,并且具有在其表面上选择性地可渗透氢气的渗透选择膜和用于使分离的气体通过渗透选择膜的排放出口。选择性渗透膜反应器还包括一个包含重整催化剂的层,该重整催化剂促进乙醇的重整,因此,由下式定义的β的范围为0.05至20:<?in-line-formulae description =“在线表达式” end =“ lead”?> == a / b <?in-line-formulae description =“在线表达式” end =“ tail”?> < UnorderedList id =“ ul0001” listStyle =“ none”> 其中a表示重整催化剂层的体积[cm 3 ],b表示选择性渗透膜的面积[cm 2 ]。

著录项

  • 公开/公告号US7560090B2

    专利类型

  • 公开/公告日2009-07-14

    原文格式PDF

  • 申请/专利权人 TOSHIYUKI NAKAMURA;NOBUHIKO MORI;

    申请/专利号US20070956733

  • 发明设计人 NOBUHIKO MORI;TOSHIYUKI NAKAMURA;

    申请日2007-12-14

  • 分类号C01B3/22;B01D53/22;

  • 国家 US

  • 入库时间 2022-08-21 19:32:03

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