渗透
渗透
膜
努森扩散
沸石
化学工程
气体分离
材料科学
扩散
选择性
分子筛
膜技术
化学
有机化学
催化作用
生物化学
热力学
物理
工程类
作者
Hua Liu,Xuechao Gao,Shengxian Wang,Zhou Hong,Xuerui Wang,Xuehong Gu
标识
DOI:10.1016/j.seppur.2021.118611
摘要
High-silica CHA (SSZ-13) zeolite membranes exhibit great potential for CO2 separation. However, the practical application is significantly hindered by the high investment cost. Here, we synthesized SSZ-13 zeolite membranes on four-channel hollow fibers with pore size of 150 nm, 370 nm and 600 nm, respectively. The CO2/CH4 selectivity of 127 ± 11 as well as CO2 permeance of (3.1 ± 0.6) × 10-7 mol m−2 s−1 Pa−1 was achieved on the membranes synthesized on the hollow fibers with 150 nm pore size at 433 K for 96 h. The single gas permeation was quantitively assigned to evaluate surface diffusion, Knudsen diffusion and viscous flow through the as-synthesized membranes. The permeation of small molecules (e.g., CO2 and N2) is mainly contributed by the zeolitic pores, however, the permeation of relatively big molecule (e.g., CH4) is more sensitive to the non-zeolitic pores. For the membranes with αCO2/CH4 of 130 and 48, the non-zeolitic pores contributed 24.7% and 69% of CH4 permeance, respectively.
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