Lasseuguette Elsa, Ferrari Maria-Chiara
School of Engineering, University of Edinburgh, Robert Stevenson Rd., Edinburgh EH9 3FB, United Kingdom.
Ind Eng Chem Res. 2024 Nov 11;63(46):20356-20364. doi: 10.1021/acs.iecr.4c03086. eCollection 2024 Nov 20.
Membrane-based gas separation processes are a technology in continuous evolution. Various types of polymer membranes have been developed, many exhibiting high CO permeability and selective properties over competing gases such as N and CH. In order to be competitive, membranes must be less-expensive, more stable, and more efficient, and their production must be scalable. One solution is to develop thin-film composites with mixed-matrix membranes (TFC_MMM) that have the potential to boost productivity while maintaining low costs. In this work, TFC_MMMs containing Matrimid mixed with 12 wt % ZIF-94 were prepared by kiss coating on a porous support. The SEM analysis showed that defect-free membranes with a 3 μm selective layer have been obtained. At 1 bar, the addition of ZIF resulted in improved the separation performance for the CO/N pair, with CO permeance of 4 GPU and CO/N selectivity of 40, surpassing neat TFC-Matrimid (CO permeance ≈ 3 GPU, CO/N selectivity ≈ 29). The use of ZIF-94 also had a stabilizing effect on the membranes against CO plasticization at high pressure.
基于膜的气体分离工艺是一种不断发展的技术。已经开发出了各种类型的聚合物膜,其中许多在对诸如氮气和甲烷等竞争气体方面表现出高的二氧化碳渗透性和选择性。为了具有竞争力,膜必须更便宜、更稳定、更高效,并且其生产必须具有可扩展性。一种解决方案是开发具有混合基质膜的薄膜复合材料(TFC_MMM),这种材料有可能在保持低成本的同时提高生产率。在这项工作中,通过在多孔载体上进行热压涂层制备了含有12 wt% ZIF-94的Matrimid混合的TFC_MMM。扫描电子显微镜分析表明,已获得具有3μm选择性层的无缺陷膜。在1巴压力下,添加ZIF提高了二氧化碳/氮气对的分离性能,二氧化碳渗透率为4 GPU,二氧化碳/氮气选择性为40,超过了纯TFC-Matrimid(二氧化碳渗透率≈3 GPU,二氧化碳/氮气选择性≈29)。使用ZIF-94对膜在高压下抵抗二氧化碳增塑也有稳定作用。