posted on 2017-10-26, 00:00authored byZhuonan 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.