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CO2 separation of fluorinated 6FDA-based polyimides, performance-improved ZIF-incorporated mixed matrix membranes and gas permeability model evaluations.
- 1.0564059 - ÚCHP 2023 RIV GB eng J - Článek v odborném periodiku
Ahmad, M. Z. - Izák, Pavel - Fíla, V.
CO2 separation of fluorinated 6FDA-based polyimides, performance-improved ZIF-incorporated mixed matrix membranes and gas permeability model evaluations.
Journal of Environmental Chemical Engineering. Roč. 10, č. 6 (2022), č. článku 108611. ISSN 2213-2929. E-ISSN 2213-3437
Grant CEP: GA MŠMT(CZ) EF16_026/0008413; GA MŠMT(CZ) LTAUSA19038
Institucionální podpora: RVO:67985858
Klíčová slova: 6FDA-based polyimides * CO 2 separation * Maxwell
Obor OECD: Chemical process engineering
Impakt faktor: 7.7, rok: 2022
Způsob publikování: Open access s časovým embargem
In this study, we compare a newly introduced high free volume fluorinated 6FDA-polyimide, namely 6FDA-bisP, with excellent gas separation properties (CO2 permeability, PCO2 of 35.3 Barrer, CO2/CH4 selectivity, alpha CO2/CH4 of 25.5) to the well-investigated, lower free volume 6FDA-ODA (PCO2 = 25.9 Barrer, alpha CO2/CH4 = 20.6). Their gas separation performances were improved in the form of mixed matrix membranes (MMMs) with size sieving zeolitic imidazolate framework (ZIF-8, particle range of <160 nm) addition between 5 and 20 wt% loadings. XRD, BET, FTIR, TGA, DSC, SEM, and TEM were used to characterize the nanoparticles and MMMs. Solid density was obtained from He pycnometry analysis (pressurized cycle test between 2 and 20 bar at 20 <degrees>C) to calculate the free fractional volume (FFV). Using an equimolar CO2 and CH4 mixture, gas separation performance was evaluated at a constant 5 bar, at 25 degrees C. The optimum loading was achieved at 15 wt% for 6FDA-bisP with MMM performance of PCO2 = 81.2 Barrer and alpha CO2/CH4 = 35.0, whereas 10 wt% for 6FDA-ODA (PCO2 = 42.2 Barrer, alpha CO2/CH4 = 44.8). The MMMs showed superior performances than the currently relevant polymers in industrial separation processes. Four different gas permeability models: Maxwell, Maxwell-Wagner-Sillar, Higuchi and Lewis Nielsen, were utilized to analyze the obtained data.
Trvalý link: https://hdl.handle.net/11104/0335804
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