CIESC Journal

• SEPARATION SCIENCE & ENGINEERING • 上一篇    下一篇

钯复合膜的制备及其在氢气氮气分离中的应用

张科1; 高会元1,3; 芮泽宝1; 林跃生1,2; 李永丹1   

  1. 1 Department of Catalysis Science and Technology, School of Chemical Engineering, Tianjin University, Tianjin 300072, China
    2 Department of Chemical and Materials Engineering, Arizona State University, Tempe, AZ 85287-1066, USA
    3 Department of Applied Chemistry, School of Chemical Engineering and Biological Technology, Hebei Polytechnic University, Tangshan 063009, China
  • 收稿日期:2006-11-20 修回日期:1900-01-01 出版日期:2007-10-28 发布日期:2007-10-28
  • 通讯作者: 张科

Preparation of thin palladium composite membranes and application to hydrogen/nitrogen separation

ZHANG Ke1; GAO Huiyuan1,3; RUI Zebao1; LIN Yuesheng1,2; LI Yongdan1   

  1. 1 Department of Catalysis Science and Technology, School of Chemical Engineering, Tianjin University, Tianjin 300072, China
    2 Department of Chemical and Materials Engineering, Arizona State University, Tempe, AZ 85287-1066, USA
    3 Department of Applied Chemistry, School of Chemical Engineering and Biological Technology, Hebei Polytechnic University, Tangshan 063009, China
  • Received:2006-11-20 Revised:1900-01-01 Online:2007-10-28 Published:2007-10-28
  • Contact: ZHANG Ke

摘要: Thin palladium composite membranes were prepared by modified electroless plating method on α-alumina supports and a dense Pd/α-Al2O3 composite membrane with high hydrogen flux, good selectivity for hydrogen was obtained. It was tested in a single gas permeation system for hydrogen permeance and hydrogen selectivity over nitrogen. The hydrogen permeance of the corresponding membrane was as high as 2.45 10-6mol•m-2•s-1•Pa-1 and H2/N2 selectivity over 700 at 623K and a pressure difference of 0.1MPa. The main resistance of the composite membrane to H2 permeation lies in the aluminum ceramic support rather than the thin Pd layer.

关键词: palladium membrane;non-electrical plating;hydrogen separation

Abstract: Thin palladium composite membranes were prepared by modified electroless plating method on α-alumina supports and a dense Pd/α-Al2O3 composite membrane with high hydrogen flux, good selectivity for hydrogen was obtained. It was tested in a single gas permeation system for hydrogen permeance and hydrogen selectivity over nitrogen. The hydrogen permeance of the corresponding membrane was as high as 2.45 10-6mol•m-2•s-1•Pa-1 and H2/N2 selectivity over 700 at 623K and a pressure difference of 0.1MPa. The main resistance of the composite membrane to H2 permeation lies in the aluminum ceramic support rather than the thin Pd layer.

Key words: palladium membrane, non-electrical plating, hydrogen separation