Guoshu Gao, Yumeng Zhao, Peng Zhu, Cun Liu, Xiongfu Zhang, Feichao Wu and Guohui Yang
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引用次数: 0
摘要
分子筛咪唑酸框架-67 (ZIF-67)膜具有刚性微孔和优异的稳定性,在甲醇/叔丁基醚(MeOH/MTBE)混合物的渗透蒸发分离中具有很大的应用潜力。然而,由于ZIF-67在散装溶液中的高成核率,制备高质量的ZIF-67膜仍然具有挑战性。在此,我们报告了通过浸渍涂层法在衬底上引入钴-乙二醇配合物(Co-EG)层的自转化制备高质量的ZIF-67管状膜。高活性的Co-EG模板层会诱导ZIF-67晶粒在衬底表面结晶生长,在室温下形成致密的ZIF-67膜。制备的MOF膜对14.3 wt%的MeOH/MTBE混合物具有良好的分离性能,总通量为2.92 kg m−2 h−1,分离因子为8945。此外,得益于Co-EG层作为锚定介质的作用,还实现了出色的长期运行稳定性。
Fabrication of high-quality ZIF-67 tubular membranes by the self-conversion of a Co–EG layer for methanol/tert-butyl ether separation†
Zeolitic imidazolate framework-67 (ZIF-67) membranes, with rigid micropores and excellent stability, show great potential in the pervaporation separation of methanol/tert-butyl ether (MeOH/MTBE) mixtures. However, it remains challenging to fabricate high-quality ZIF-67 membranes due to the high nucleation rate of ZIF-67 in the bulk solutions. Herein, we report the fabrication of a high-quality ZIF-67 tubular membrane by the self-conversion of a cobalt–ethylene glycol complex (Co–EG) layer that was introduced on the substrate by a dip-coating method. The highly reactive Co–EG template layer would induce the crystallization and growth ZIF-67 grains on the substrate surface, resulting in the formation of a dense ZIF-67 membrane at room temperature. The obtained MOF membrane displays an excellent separation performance in separating 14.3 wt% MeOH/MTBE mixture, presenting a total flux of 2.92 kg m−2 h−1 and separation factor of 8945. Besides, an outstanding long-term operating stability is also achieved, benefiting from the Co–EG layer acting as an anchoring medium.