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We investigated eight representative metal–organic frameworks for methane storage using molecular simulation. Validated force fields were used to calculate the amount adsorbed for pure methane and its mixtures with CO2 and H2O at 5.8 and 65 bar at 298 K within the composition limits specified for natural gas. Within the analyzed concentrations, the MOFs without open metal sites were minimally influenced by the presence of CO2 and H2O. However, for the MOFs with open metal sites, the presence of these species proved to be harmful. We found that concentrations as low as 25 ppm of water can reduce the delivered volume of methane by more than 20%. A detailed analysis of the adsorption mechanisms leading to this poisoning is presented. These results highlight the possible limitations of MOFs with open metal sites for use in natural gas storage. [ABSTRACT FROM AUTHOR]

Diffusion of methane, ethane, propane and n-butane was studied within the micropores of several metal-organic frameworks (MOFs) of varying topologies, including the MOFs PCN-14, NU-125, NU-1100 and DUT-49. Diffusion coefficients of the pure components, as well as methane/ethane, methane/propane and methane/butane binary mixtures, were calculated using molecular dynamics simulations to understand the effect of the longer alkanes on uptake of natural gas in MOFs. The calculated self-diffusion coefficients of all four components are on the order of 10 −8 m 2 /s. The diffusion coefficients of the pure components decrease as a function of chain length in all of the MOFs studied and show different behaviour as a function of loading in different MOFs. The self-diffusivities follow the trend D PCN-14 NU-125≈NU-1100>DUT-49. By comparing the diffusion of pure methane and methane mixtures with the higher alkanes, it is observed that the diffusivity of methane is unaffected by the presence of the higher alkanes in the MOFs considered, indicating that the diffusion path of methane is not blocked by the higher alkanes present in natural gas. [ABSTRACT FROM AUTHOR]