渗透
膜
沸石
材料科学
化学工程
气体分离
色谱法
离心
化学
渗透
有机化学
催化作用
生物化学
工程类
作者
Yue Zhou,Peng Du,Zhifei Song,Xinfa Zhang,Yu Liu,Yuting Zhang,Xuehong Gu
标识
DOI:10.1016/j.memlet.2023.100038
摘要
All-silica DD3R zeolite has been recognized as a promising CO2-selective membrane material owing to its appropriate pore size (0.36 nm × 0.44 nm), strong hydrophobicity, excellent thermal and chemical stabilities. In order to reduce membrane cost, it is meaningful to synthesize thin DD3R zeolite membranes that possess high gas permeance. In this work, high-performance DD3R zeolite membranes were synthesized on TiO2/α-Al2O3 composite hollow fibers by secondary growth method. Sigma-1 zeolite seeds were ball-milled and then fractionated into different-sized seeds by gradient centrifugation. Smaller seed particles were collected after centrifuged at higher rotation speed rate. A very thin and dense DD3R zeolite membrane (thickness: 1.2 μm) was synthesized by using the smallest seeds (ZS4) with average particle size of 163 nm, which were obtained from the supernatant of the third centrifugation at 11000 rpm. The as-synthesized membranes were employed in separation of equimolar CO2/CH4 mixture. Compared with the original ball-milled seeds (ZS1)-induced membrane, the seed ZS4-induced membrane exhibited an improved CO2 permeance of 1.2 × 10−7 mol m−2 Pa−1 s−1 by 62%. All the resultant membranes performed good CO2/CH4 separation selectivities between 262 and 364.
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