ZIF‐8 membrane has the potential for CO2/CH4 separation based on size exclusion. But if traditionally prepared by solvothermal methods, it shows only negligible selectivity due to the linker mobility. Here, ≈500 nm‐thin hybrid ZIF‐7x‐8 membranes with suppressed linker mobility and narrowed window aperture are prepared by a fast current‐driven synthesis (FCDS) within 20 min. The in situ electric field during FCDS allows the formation of stiffened ZIF‐8_Cm as parent skeleton and the mixed‐linker strategy is applied to narrow the aperture size simultaneously. The ZIF‐722‐8 membrane shows significantly sharpened molecular sieving for CO2/CH4 with a separation factor above 25, which soared tenfold compared with other unmodified ZIF‐8 membranes. Additionally, the membrane shows exceptional separation performance for H2/CH4 and CO2/N2, with separation factors of 71 and 20, respectively. After 180 h temperature swing operation, it still maintains the excellent separation performance.
Separation is one of the most energy-intensive
processes in the
chemical industry, and membrane-based separation technology helps
to reduce the energy consumption dramatically. Supported metal–organic
framework (MOF) layers hold great promise as a molecular sieve membrane,
yet only a few MOF membranes showed the expected separation performance.
The main reasons include e.g. nonselective grain boundary transport
or the flexible MOF framework, especially the inevitable linker rotation.
Here, we propose a crystal engineering strategy that balances the
grain boundary structure and framework flexibility in Co–Zn
bimetallic zeolitic imidazolate framework (ZIF) membranes and exploit
their contributions to the improvement of membrane quality and separation
performance. It reveals that a good balance between the two trade-off
factors enabled a “sweet spot” that offers the best
C3H6/C3H8 separation factor
up to 200.
Metal–organic
framework (MOF) membranes have enormous potential
in separation applications. There are several MOF membranes grown
on polymer substrates aimed for scale-up, but their brittleness hampers
any industrial application. Herein, intergrown continuous polypropylene
(PP)-supported ZIF-8 membranes have been successfully synthesized
via fast current-driven synthesis (FCDS) within 1 h. The PP-supported
ZIF-8 membranes exhibit a promising separation factor of 122 ±
13 for binary C3H6–C3H8 mixtures combined with excellent flexibility behavior. The
C3H6/C3H8 separation performance
of the PP-supported ZIF-8 membrane was found to be constant after
bending the supported ZIF-8 film with a curvature of 92 m–1. This outstanding mechanical property is crucial for practical applications.
Moreover, we further synthesized ZIF-8 membranes on various polymer
substrates and even polymer hollow fibers to demonstrate the production
scalability.
Ebola virus (EBOV) belongs to the
Filoviridae family, which can
cause severe hemorrhagic fever in humans and nonprimates. The neutralization
of EBOV by monoclonal antibody (mAb) ADI-15946 was reported recently.
In the present study, the molecular interactions between the receptor
GPcl of EBOV and ADI-15946 were studied by molecular dynamics (MD)
simulation and molecular mechanics–Poisson–Boltzmann
surface area (MM–PBSA) analysis. Hydrophobic interaction was
identified as the main driving force for the binding of ADI-15946
on EBOV. Moreover, the contribution of each amino acid residue for
the binding was evaluated. Then, an affinity binding model (ABM) was
constructed using the residues favorable for the binding, including
Y107, F108, D109, W110, and R113. The biomimetic design of neutralizer
against EBOV according to the ABM of ADI-15946 was then performed,
followed by screening using docking, structural similarity. Two neutralizers
YFDWHMR and YFDWRYR were obtained, which were proven to be capable
of strong binding on GPcl and then neutralizing GPcl. These results
would be helpful for the development of neutralizers for Ebola virus.
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