渗透
膜
沸石
渗透
选择性
化学工程
化学
材料科学
催化作用
有机化学
生物化学
工程类
作者
Lin Wang,Chun Zhang,Xuechao Gao,Peng Li,Jiang Ji,Xuehong Gu
标识
DOI:10.1016/j.memsci.2017.06.004
摘要
A dilute synthesis precursor was developed to prepare high-quality DDR zeolite membranes on α-Al2O3 four-channel hollow fibers by secondary growth method. However, the as-membranes were susceptible to crack during high temperature activation (>873 K) for the template removal. A molecular simulation demonstrated that a large contraction of ~ 5% occurred for the DDR zeolite framework after template removal. Ozone environment was employed for membranes activation at low temperature (473 K) to prevent the formation of cracks. The occluded template in zeolite cages was successfully removed by this way and high quality DDR zeolite membranes were achieved reproducibly without any cracks. The membranes were further evaluated for single gas permeation and separation of CO2/CH4 mixture. The ideal selectivities for CO2/CH4, CO2/N2, CO2/C3H8, CO2/H2, N2/CH4 and O2/N2 were 305, 32, 1500, 5, 10 and 1.7, respectively. For the separation of equimolar CO2/CH4 mixture, a high selectivity of 500 and CO2 permeance of 3.5×10−8 mol m−2 s−1 Pa−1 could be achieved. The membranes also exhibited high stability in wet environment. A stable permeance of 3.5×10−8 mol m−2 s−1 Pa−1 and selectivity of 140 could be achieved during 40 h test for the separation of CO2/CH4 mixture containing 1.5% vapor at 353 K.
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