A Copper-Based Metal–Organic Framework for Selective Separation of C2 Hydrocarbons from Methane at Ambient Conditions: Experiment and Simulation

C2 hydrocarbon separation from methane represents a technological challenge for natural gas upgrading. Herein, we report a new metal–organic framework, [Cu2L­(DEF)2]·2DEF (UNT-14; H4L = 4,4′,4″,4‴-((1E,1′E,1″E,1‴E)-benzene-1,2,4,5-tetrayltetrakis­(ethene-2,1-diyl))­tetrabenzoic acid; DEF = N,N-diethylformamide; UNT = University of North Texas). The linker design will potentially increase the surface area and adsorption energy owing to π­(hydrocarbon)−π­(linker)/M interactions, hence increasing C2 hydrocarbon/CH4 separation. Crystallographic data unravel an sql topology for UNT-14, whereby [Cu2(COO)4]···[L]4– paddle-wheel units afford two-dimensional porous sheets. Activated UNT-14a exhibits moderate porosity with an experimental Brunauer–Emmett–Teller (BET) surface area of 480 m2 g–1 (vs 1868 m2 g–1 from the crystallographic data). UNT-14a exhibits considerable C2 uptake capacity under ambient conditions vs CH4. GCMC simulations reveal higher isosteric heats of adsorption (Q st) and Henry’s coefficients (K H) for UNT-14a vs related literature MOFs. Ideal adsorbed solution theory yields favorable adsorption selectivity of UNT-14a for equimolar C2H n /CH4 gas mixtures, attaining 31.1, 11.9, and 14.8 for equimolar mixtures of C2H6/CH4, C2H4/CH4, and C2H2/CH4, respectively, manifesting efficient C2 hydrocarbon/CH4 separation. The highest C2 uptake and Q st being for ethane are also desirable technologically; it is attributed to the greatest number of “agostic” or other dispersion C–H bond interactions (6) vs 4/2/4 for ethylene/acetylene/methane.