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Dual-Channel, Molecular-Sieving Core/Shell ZIF@MOF Architectures as Engineered Fillers in Hybrid Membranes for Highly Selective CO<sub>2</sub> Separation

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posted on 2017-10-26, 00:00 authored by Zhuonan Song, Fen Qiu, Edmond W. Zaia, Zhongying Wang, Martin Kunz, Jinghua Guo, Michael Brady, Baoxia Mi, Jeffrey J. Urban
A novel core/shell porous crystalline structure was prepared using a large pore metal organic framework (MOF, UiO-66-NH<sub>2</sub>, pore size, ∼ 0.6 nm) as core surrounded by a small pore zeolitic imidazolate framework (ZIF, ZIF-8, pore size, ∼ 0.4 nm) through a layer-by-layer deposition method and subsequently used as an engineered filler to construct hybrid polysulfone (PSF) membranes for CO<sub>2</sub> capture. Compared to traditional fillers utilizing only one type of porous material with rigid channels (either large or small), our custom designed core/shell fillers possess clear advantages via pore engineering: the large internal channels of the UiO-66-NH<sub>2</sub> MOFs create molecular highways to accelerate molecular transport through the membrane, while the thin shells with small pores (ZIF-8) or even smaller pores generated at the interface by the imperfect registry between the overlapping pores of ZIF and MOF enhance molecular sieving thus serving to distinguish slightly larger N<sub>2</sub> molecules (kinetic diameter, 0.364 nm) from smaller CO<sub>2</sub> molecules (kinetic diameter, 0.33 nm). The resultant core/shell ZIF@MOF and as-prepared hybrid PSF membranes were characterized by transmission electron microscopy, X-ray diffraction, wide-angle X-ray scattering, scanning electron microscopy, Fourier transform infrared, thermogravimetric analysis, differential scanning calorimetry, and contact angle tests. The dependence of the separation performance of the membranes on the MOF/ZIF ratio was also studied by varying the number of layers of ZIF coatings. The integrated PSF-ZIF@MOF hybrid membrane (40 wt % loading) with optimized ZIF coating cycles showed improved hydrophobicity and excellent CO<sub>2</sub> separation performance by simultaneously increasing CO<sub>2</sub> permeability (CO<sub>2</sub> permeability of 45.2 barrer, 710% higher than PSF membrane) and CO<sub>2</sub>/N<sub>2</sub> selectivity (CO<sub>2</sub>/N<sub>2</sub> selectivity of 39, 50% higher than PSF membrane), which is superior to most reported hybrid PSF membranes. The strategy of using dual-channel molecular sieving core/shell porous crystals in hybrid membranes thus provides a promising means for CO<sub>2</sub> capture from flue gas.

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