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不锈钢金属网上L型分子筛膜的连续生长及气体渗透性能
引用本文:张金磊,赵晴,刘佳,孙福兴.不锈钢金属网上L型分子筛膜的连续生长及气体渗透性能[J].高等学校化学学报,2013,34(4):771-775.
作者姓名:张金磊  赵晴  刘佳  孙福兴
作者单位:1. 吉林大学无机合成与制备化学国家重点实验室, 长春 130012; 2. 吉林大学中日联谊医院, 长春 130033
基金项目:国家自然科学基金(批准号:20831002)资助.
摘    要:选取不锈钢金属网作为成膜载体, 采用预涂晶种的方法, 研究了L型分子筛晶种在水热条件下二次生长成膜的过程. 对成膜条件进行了详细的考察, 并讨论了反应液的碱度及反应时间对L型分子筛膜形成的影响. 利用扫描电子显微镜(SEM)对L型分子筛膜的形貌进行了表征. 通过优化反应条件, 得到了致密、 连续、 纯相、 均匀的L型分子筛膜, 厚度约为20 μm. 单组分气体渗透测试结果表明, 在室温和常压下, L型分子筛膜对N2气和H2气的渗透速率分别为8.39×10-8 和6.96×10-7 mol·m-2·s-1·Pa-1, 从而计算出膜对H2/N2混合气体的理想分离系数为8.3. 双组分气体渗透测试结果表明, 温度的升高会导致膜对H2气和N2气的渗透速率增加及H2/N2分离系数的减小.

关 键 词:L型分子筛膜  反应条件  气体分离  
收稿时间:2012-10-31

Growth and Gas Permeation Properties of Continuous L-type Zeolite Membrane on Stainless Steel Net
ZHANG Jin-Lei,ZHAO Qing,LIU Jia,SUN Fu-Xing.Growth and Gas Permeation Properties of Continuous L-type Zeolite Membrane on Stainless Steel Net[J].Chemical Research In Chinese Universities,2013,34(4):771-775.
Authors:ZHANG Jin-Lei  ZHAO Qing  LIU Jia  SUN Fu-Xing
Institution:1. State Key Laboratory of Inorganic Synthesis and Preparative Chemistry, Jilin University, Changchun 130012, China; 2. China-Japan Union Hospital, Jilin University, Changchun 130033, China
Abstract:Growth of L-type zeolite membrane on stainless steel net by the secondary hydrothermal growth was studied under different conditions. The effects of the alkalinity of the reaction solution and the reaction time on the formation of L-type zeolite membrane were discussed via the observation through scanning electron microscopy technique. The continuous uniform phase-pure L-type zeolite membrane was obtained with a thickness of about 20 μm. Single gas permeation measurement on the as-synthesized L-type membrane demonstrates that the permeance of N2 and H2 are 8.39×10-8 and 6.96×10-7 mol·m-2·s-1·Pa-1 respectively, indicating an ideal selectivity for H2/N2 of 8.3. Binary gas permeation measurement demonstrates that the increase of temperature would strengthen the permeation of N2 and H2, but decrease the separation factor of H2/N2.
Keywords:L-type zeolite membrane  Reaction condition  Gas separation
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