渗透汽化
膜
微型多孔材料
化学工程
立方氧化锆
气体分离
膜技术
材料科学
选择性
介孔材料
色谱法
化学
有机化学
渗透
催化作用
陶瓷
生物化学
工程类
作者
Tim Van Gestel,Frans Velterop,Wilhelm A. Meulenberg
标识
DOI:10.1016/j.seppur.2020.118114
摘要
Hybrid organosilica membranes have great potential for realizing high-flux, high-selectivity gas separation and pervaporation. Current membranes, however, have one major problem: the intermediate layers between the selective layer and the porous support are made of unstable γ-alumina. In this article, a strongly improved membrane set-up based on mesoporous stabilized zirconia (8YSZ) intermediate layers is reported. This novel membrane showed selectivities in the range of 20–30 for different CO2/N2 mixtures and accompanying CO2 permeances of 1.5–4 m3/(m2.h.bar). In pervaporation tests with water/isopropanol and water/butanol mixtures (5 wt% water), the membrane selectively separated water (separation factor ~150 – 600) and an excellent flux of ~5 kg m-2h−1 was achieved at 70 °C. These results represent an important step towards the industrial application of hybrid silica membranes in applications such as pervaporation as well as the selective removal of CO2. The analysis also shows for the first time that effective gas separation and pervaporation is realized when γ-alumina is substituted for another, more stable membrane material.
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