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.
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http://www.ncbi.nlm.nih.gov/pmc/articles/PMC11583212 | PMC |
http://dx.doi.org/10.1021/acs.iecr.4c03086 | DOI Listing |
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