渗透
渗透
沸石
膜
热扩散率
化学
活化能
化学工程
扩散
分子筛
化学气相沉积
气体扩散
物理化学
热力学
有机化学
催化作用
吸附
电极
工程类
物理
生物化学
作者
Masakoto Kanezashi,Jessica O’Brien-Abraham,Jerry Y S Lin,Kenji Suzuki
出处
期刊:Aiche Journal
[Wiley]
日期:2008-04-22
卷期号:54 (6): 1478-1486
被引量:195
摘要
Abstract DDR‐type zeolite membranes were prepared by the secondary growth method on porous α‐alumina disk, followed by on‐stream counter diffusion chemical vapor deposition modification to eliminate the intercrystalline micropores. Single gas permeation of He, H 2 , CO 2 , and CO through this zeolite membrane before and after CVD modification was measured in 25–500°C. Intracrystalline diffusivities for these four gases in DDR‐type zeolite were obtained from the permeation data above 300°C to examine the effects of the size and molecular weight of permeating gases on diffusion and permeation rate for this zeolite membrane. For the unmodified DDR‐type zeolite membrane with presence of a small amount intercrystalline micropores the diffusivity (or permeance) with a low activation energy depends on both the size and molecular weight of permeating gases. For the CVD‐modified DDR‐type zeolite membrane with intercrystalline micropores eliminated, the activation energy for diffusion and diffusivity increases with increasing molecular size of the permeating gases. © 2008 American Institute of Chemical Engineers AIChE J, 2008.
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