The edge-functionalization enhances the competitive adsorption of CO2over CH4in NPCs by improving pore topology, electronegativity, adsorption energy, and electrostatic contribution.
Strategies to enhance CO 2 capture and separation based on state-of-the-art adsorbent materials have been proposed by topological structure design, chemical doping, chemical functionalization, open metal sites, and electric fields. This review presents a constructive way for the design and screening of novel adsorbent materials.
A porous Cu metal–organic framework (1) based on a pentacarboxylate ligand and paddlewheel SBU was synthesized and structurally characterized. Complex 1 possesses a NbO-type framework with uncoordinated –COO− groups, resulting in its good selectivity for CO2/N2 (36) and CO2/CH4 (12) as well as a large CO2-uptake capacity of 140 cm3 g−1 at 273 K and 1 bar. Grand Canonical Monte Carlo (GCMC) simulations revealed that strong CO2 adsorption sites exist near the open CuII sites and the uncoordinated –COO− groups. Significantly, complex 1 exhibits water resistance and selective adsorption of cationic methylene blue (MB+) in aqueous solution and the adsorbed MB+ can be released in saturated NaCl solution, making it also a promising porous material for charge and pore-size dependent large-molecule capture and separation. The existence of coordinatively unsaturated metal sites as well as the exposed –COO− groups in the framework of 1 is responsible for its selective gas adsorption and dye separation.
The storage and separation of hydrocarbons is of great importance for the petrochemical industry. Herein, we report a fluorine-functionalized microporous indium (In) metal–organic framework (UPC-104) for light hydrocarbon storage and separation. UPC-104 can be stable up to 300 °C, and can retain its framework in acidic and alkaline aqueous solutions (pH 1–11). Remarkably, the material exhibits very high H2 (230.8 cm3 g−1, 2.06 wt% at 77 K and 1 bar), C2H2 (187.0 cm3 g−1 at 273 K and 1 bar), and C3H6/C3H8 adsorption capacity (276.5 cm3 g−1 and 250.4 cm3 g−1 for C3H6 and C3H8 at 273 K and 1 bar), and shows potential for the separation of light hydrocarbons (C2H2, C2H4, C2H6, C3H6, C3H8, n-C4H10, and i-C4H10 relative to CH4), as shown by single component gas sorption and selectivity calculations.