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Cited 11 time in webofscience Cited 11 time in scopus
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Highly concentrated multivariate ZIF-8 mixed-matrix hollow fiber membranes for CO2 separation: Scalable fabrication and process analysis

Authors
An, HeseongJung, WonhoShin, Ju HoShin, Min ChangPark, Jung HoonLee, JinwonLee, Jong Suk
Issue Date
Oct-2023
Publisher
ELSEVIER
Keywords
Mixed matrix hollow fiber membranes; CO2 separation; Dip coating; Multivariate ZIF-8; Process analysis
Citation
Journal of Membrane Science, v.684, pp 1 - 12
Pages
12
Indexed
SCIE
SCOPUS
Journal Title
Journal of Membrane Science
Volume
684
Start Page
1
End Page
12
URI
https://scholarworks.dongguk.edu/handle/sw.dongguk/21133
DOI
10.1016/j.memsci.2023.121875
ISSN
0376-7388
1873-3123
Abstract
Here, we report on the fabrication of mixed matrix hollow fiber membranes (MMHFMs) for CO2 separation using highly-concentrated 6FDA-DAM/triple-ligand, amine-modulated zeolitic imidazolate framework-8 (TAZIF-8) (60/40 w/w) via a dip coating process. The application of a & gamma;-alumina interlayer serves a dual purpose of reducing the infiltration of the 6FDA-/TAZIF-8 coating solution into the porous & alpha;-alumina support, while also providing a smooth surface for the support. Importantly, the co-solvent comprising N-methyl-2-pyrrolidone and dichloromethane further inhibits the formation of defects by maintaining an appropriate balance of volatility and polarity. This balanced combination is crucial in promoting phase separation and facilitating the dispersion of nanofillers within the polymer matrix, enabling the formation of a thin defect-free selective layer. The subse-quent 40 wt% TAZIF-8 MMHFM attains superior CO2 separation performance to most existing MMHFMs (CO2 permeance of 648 GPU and CO2/N2 and CO2/CH4 selectivity of 39.0 and 34.2, respectively). Furthermore, it maintains excellent CO2 separation performance over 120 d owing to good interfacial interaction between 6FDA-DAM and TAZIF-8s. Last, but not least, our process analysis reveals that the introduction of the TAZIF-8 MMHFM into the first stage of a dual-stage membrane process can improve the total energy demand for post-combustion CO2 capture due to its excellent CO2/N2 selectivity. Our current study provides significant progress toward the industrial application of post-combustion CO2 capture.
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