Incorporating
metal–organic frameworks (MOFs) into the thin
layer of thin-film composite (TFC) membranes is an effective way of
improving the CO2/CH4 separation performance.
In this study, porous polyethersulfone (PES) membranes were surface-coated
with a novel CO2-permeable layer consisting of CO2-philic Pebax and nickel-based MOF particles. The MOF particles were
synthesized using nickel(II) acetate tetrahydrate as a metal source
and 2-amino-1,4-dicarboxybenzene (NH2-BDC) as an organic
linker. The properties and performance of the MOFs and synthesized
membranes were assessed using analytical techniques including differential
scanning calorimetry (DSC), thermogravimetric analysis (TGA), field-emission
scanning electron microscopy (FE-SEM), and dynamic light scattering
(DLS). DLS analysis showed that the MOF particle size range was in
a range of 350–650 nm. Moreover, cross-sectional FE-SEM images
depicted that a uniform and dense Pebax layer was shaped on top of
the PES substrate. Well dispersion of the particles was demonstrated
by surface FE-SEM imaging. DSC analysis showed that embedding Ni-NH2-BDC MOF particles into the Pebax-1657 film increased the
crystallinity degree and the glass-transition temperature (T
g) of resulted membranes. To evaluate the membrane’s
separation performance, permeation experiments were performed with
CO2, CH4, and CO2/CH4 mixtures
at ambient temperature. Embedding 5 wt % Ni-based MOF particles improved
the CO2 permeability and CO2/CH4 selectivity
from 19.05 Barrer and 32.2 to 31.55 Barrer and 94, respectively, compared
to MOF-free membranes. Loading MOF particles into the Pebax matrix
also improved the real gas separation factor. The obtained results
demonstrate the great potential of the fabricated TFC membranes for
gas separation.
In this study, Cu-BTC (copper(II) benzene-1,3,5-tricarboxylate) metal-organic frameworks (MOFs) were incorporated into the structure of polysulfone (PSf) ultrafiltration (UF) membranes to improve the membrane performance for landfill leachate treatment, whereby different concentrations of Cu-BTC (0.5, 1, 1.5, 2 wt%) were added to the PSf casting solution. The successful incorporation of Cu-BTC MOFs into the modified membranes was investigated by field emission scanning electron microscopy (FE-SEM) and energy dispersive X-ray (EDX). The Cu-BTC-modified PSf membranes showed higher performance in terms of flux and rejection, as compared to the neat PSf membrane. For example, the pure water flux (PWF) of neat membrane increased from 111 to 194 L/m2h (LMH) by loading 2 wt% Cu-BTC into the membrane structure, indicating 74% improvement in PWF. Furthermore, the flux of this membrane during filtration of landfill leachate increased up to 15 LMH, which indicated 50% improvement in permeability, as compared to the neat membrane. Finally, the modified membranes showed reasonable antifouling and anti-biofouling properties than the blank membrane.
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