(606e) Exploring the Effect of Intra-Chain Rigidity on Mixed-Gas Separation Performance of a Triptycene-Tröger’s Base Ladder Polymer By Atomistic Simulations
AIChE Annual Meeting
2023
2023 AIChE Annual Meeting
Separations Division
Synthesis and Characterization of Advanced Polymer Membranes for Gas and Vapor Separations
Wednesday, November 8, 2023 - 9:24am to 9:45am
Monte Carlo (MC) and Molecular Dynamics (MD) methods were employed to produce pure- and mixed-gas sorption and permeation data for CO2 and CH4 in PIM-Trip-TB. The simulated polymer density was calculated to be 1.04 ± 0.02 g/cc and compared very well with the reported experimental geometric density of 1.02 ± 0.02 g/cc.4 Experimental data availability for both sorption uptakes and gas permeability at pure- and mixed-gas conditions allowed extensive validation of our approach and models before performing further structural analysis. Accurate reproduction of both sorption and permeability data were accomplished using the all-atomistic methodology. Grand Canonical Monte Carlo (GCMC) simulations were combined with MD simulations to be able to reproduce the CO2-induced dilation of the polymer matrix during sorption. Gas transport diffusion coefficients were calculated using Maxwell-Stefan relationships, where n-th order algorithm was employed to obtain the diffusion components.6 It should be noted that, in mixed-gas conditions, ~ 3-fold increase in CO2/CH4 solubility selectivities were observed compared to the pure-gas values, as demonstrated in the experimental report.4 When gas-polymer interaction energies were analyzed, significant decrease in CH4-polymer interactions in mixed-gas conditions were observed, mainly due to preferential sorption of the CO2 molecules in the polymer. Furthermore, previously reported loss in experimental perm-selectivities under mixed-gas conditions was consistently found to be reproducible by the simulations. Diffusion simulations in mixed-gas conditions proved that diffusion selectivity of PIM-Trip-TB decreases to values as low as ~ 1, resulting in either equal, or lower perm-selectivities compared to those obtained by pure-gas simulations. Despite the intra-chain rigidity of PIM-Trip-TB, co-permeation of CO2 in mixed-gas conditions led to an increase in the CH4 diffusivity, which resulted in the decrease in perm-selectivity.
After the accuracy of our methods was extensively proved by comparing physical and pure- and mixed-gas transport properties of PIM-Trip-TB with experimental values, in-detail structural analyses were performed. Initial structural properties of PIM-Trip-TB and structural dynamics induced by CO2 were tracked and compared. Our simulations indicated that at 10 atm CO2 partial pressure, FFV of PIM-Trip-TB increases by ~13% to 0.32 compared to the initial value of 0.28. Such an increase can directly be related to the observed increase in diffusivities considering diffusivities of gases are known to be exponentially related to FFV. The significance of the increase in free volume was demonstrated by PSD analysis. CO2-induced dilation created new free volume elements with diameters larger than CH4 in the structure which resulted in an overall shift of PSD toward larger pore sizes. Combined numerical and graphical observations led to the conclusion that FFV elements in the system were large and connected enough for the polymer to lose any size sieving capability for the CO2/CH4 gas pair. Torsion Distribution Function and Radial Distribution Function analyses proved that the intra-chain rigidity claimed for PIM-Trip-TB was correct, yet CO2-induced dilation in the structure appeared despite preserving the initial intra-chain rigidity. By combining all effects, it is clear that despite the rigid structure of the PIM-Trip-TB monomer, the polymer matrix was unable to sustain its initial packing, hence, its ideal pure-gas CO2/CH4 diffusion selectivity under mixed-gas conditions.
The results of this study highlight the importance of inter-chain rigidity â future studies focusing on the effect and possible manipulation of inter-chain rigidity should be performed to optimize advanced membrane materials for more efficient mixed-gas separation processes.
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