The CO2 Storage Capacity of the Intercalated Diaminoalkane Graphene Oxides: A Combination of Experimental and Simulation Studies

Studying of the adsorption and diffusion behaviors of methane on graphene oxide by molecular dynamics simulation

In this work, the sorption and diffusion behaviors of the methane on graphene oxide (GO) were investigated by molecular dynamics (MD) simulation. The sorption isotherms at different temperatures were calculated using the Grand Canonical Monte Carlo (GCMC) method and using the Langmuir adsorption model to fit those isotherms. To investigate the effect of the number of graphene oxide layers on the adsorption process, methane adsorption isotherms were calculated for graphene oxide with 1, 2, and 3 layers. The adsorption parameters including Langmuir adsorption constant, the entropy and the enthalpy of adsorption, collision flux, the rate of adsorption, and the rate of desorption were investigated in this work. The highest amount of adsorption calculated is related to graphene oxide three layers. The methane diffusion coefficients and diffusion activation energies were estimated at different temperatures by MD simulation coupled with Einstein relationship. The maximum diffusion coefficient calculated of methane at 348 K was 49 × 10^-10 m²/s.

Effect of Varying Amine Functionalities on CO2 Capture of Carboxylated Graphene Oxide-Based Cryogels

Graphene cryogels synthesis is reported by amine modification of carboxylated graphene oxide via aqueous carbodiimide chemistry. The effect of the amine type on the formation of the cryogels and their properties is presented. In this respect, ethylenediamine (EDA), diethylenetriamine (DETA), triethylenetetramine (TETA), were selected. The obtained cryogels were characterized by Fourier Transformed Infrared spectroscopy, thermogravimetric analysis, X-ray spectroscopy, and Scanning electron microscopy. The CO2 adsorption performance was evaluated as a function of amine modification. The results showed the best CO2 adsorption performance was exhibited by ethylenediamine modified aerogel, reaching 2 mmol g-1 at 1 bar and 298 K. While the total N content of the cryogels increased with increasing amine groups, the nitrogen configuration and contributions were determined to have more important influence on the adsorption properties. It is also revealed that the residual oxygen functionalities in the obtained cryogels represent another paramount factor to take into account for improving the CO2 capture properties of amine-modified graphene oxide (GO)-based cryogels.

Insights into the H2/CH4 Separation Through Two-Dimensional Graphene Channels: Influence of Edge Functionalization

A molecular simulation technique is employed to investigate the transport of H2/CH4 mixture through the two-dimensional (2D) channel between adjacent graphene layers. Pristine graphene membrane (GM) with pore width of 0.515~0.6 nm is found to only allow H2 molecules to enter rather than CH4, forming a molecular sieve. At pore widths of 0.64~1.366 nm, both H2 and CH4 molecules could fill into the GM channel, where the permeability of methane is more preferential than that of hydrogen with the largest CH4/H2 selectivity (1.89) at 0.728 nm. The edge functionalization by -H, -F, -OH, -NH2, and -COOH groups could significantly alter gas permeability by modifying the active surface area of the pore and tuning attractive and/or repulsive interaction with molecules at the entrance of channel. At the pore width of 0.6 nm, the H2 permeability of molecular sieve is enhanced by -H, -F, and -OH groups but restrained by -NH2, especially -COOH with a passing rate of zero. At pore widths of 0.64 and 0.728 nm, both -H and -F edge-functionalized GMs show a preferential selectivity of methane over hydrogen, while the favorable transport for GM-OH is changed from H2 molecules at 0.64 nm to CH4 molecules at 0.728 nm. For GM-NH2, it exhibits an excellent hydrogen molecular sieve at 0.64 nm and then turns into a significant H2/CH4 selectivity at 0.728 nm. Meanwhile, small H2 molecules start to enter the channel of GM-COOH at the pore width up to 0.728 nm. For the largest pore width of 1.336 nm, the influence of edge functionalization becomes small, and a comparable CH4/H2 selectivity is observed for all the considered membranes.