渗透
膜
沸石
渗透
化学工程
选择性
水蒸气
化学
气体分离
多孔性
材料科学
色谱法
有机化学
催化作用
生物化学
工程类
作者
Koji Kida,Yasushi Maeta,Katsunori Yogo
标识
DOI:10.1016/j.seppur.2017.12.060
摘要
Dense and thin pure silica CHA-type zeolite (Si-CHA) membranes have been synthesized on porous α-alumina supports and investigated for CO2 permeation and CO2/CH4 separation performance under dry and humidified conditions. Si-CHA membranes with ultra-high permeance were greatly affected by performance suppression due to concentration polarization under high pressure and low feed-rate conditions. Under high feed-rate conditions at 298 K and a feed pressure of 0.1 MPaG, the CO2/CH4 selectivity was 130 with a CO2 permeance of 4.0 × 10–6 mol/(m2 s Pa) for an equimolar CO2/CH4 dry gas mixture. The presence of water vapor significantly reduced CO2 permeance, but the performance improved as feed pressure increased. The CO2/CH4 selectivities at high pressure with and without water vapor were essentially the same.
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