Preparation of Zeolite T Membranes by a Two-Step Temperature Process for CO2 Separation

被引:29
|
作者
Zhang, Xiao-Liang [1 ]
Qiu, Ling-Fang [1 ,2 ]
Ding, Min-Zheng [1 ]
Hu, Na [1 ]
Zhang, Fei [1 ]
Zhou, Rong-Fei [1 ]
Chen, Xiang-Shu [1 ,2 ]
Kita, Hidetoshi [2 ]
机构
[1] Jiangxi Normal Univ, Coll Chem & Chem Engn, Jiangxi Inorgan Membrane Mat Engn Res Ctr, Nanchang 330022, Peoples R China
[2] Yamaguchi Univ, Grad Sch Sci & Engn, Ube, Yamaguchi 7558611, Japan
基金
中国国家自然科学基金;
关键词
PERVAPORATION PROPERTIES; HYDROTHERMAL SYNTHESIS; SYNTHESIS PARAMETERS; CLEAR SOLUTIONS; PERFORMANCE; GAS; PERMEATION; ADSORPTION; CO2/CH4; ZSM-5;
D O I
10.1021/ie4025402
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A thin and well-intergrown zeolite T membrane with high CO2 permeability and selectivity was rapidly prepared on seeded tubular supports by the two-step varying-temperature hydrothermal synthesis process (two-step method). The influence of synthesis parameters such as synthesis temperature and crystallization time during the two-step durations on crystals growth and separation performance was investigated systematically. The X-ray diffraction (XRD), scanning electron microscopy (SEM), and gas permeation measurements were used to characterize the as-synthesized membranes. Compared with the conventional hydrothermal synthesis at a constant temperature (one-step method), the two-step method is more effective to synthesize a thin and continuous zeolite membrane layer in short time, which fully covered the support surface. Membrane synthesis temperature during the two-step durations could seriously influence the crystal growth and CO2 separation properties. It was found that a lower temperature favored nucleation, while a higher crystallization temperature promoted crystallization during the two-step method, thus improving zeolite T crystal growth and membrane separation properties. The membranes prepared by the two-step method under the optimized conditions exhibited good reproducibility, high CO2 permeance, and relatively high permselectivity for the separation of CO2 from CH4 or N-2 gas mixtures. For example, CO2 permeance and CO2/CH4 selectivity of the membranes reached 6.2 X 10(-8) mol m(-2) s(-1) Pa-1 and 80 for the equimolar CO2/CH4 binary gaseous mixtures at 35 degrees C, respectively.
引用
收藏
页码:16364 / 16374
页数:11
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