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Published on: March 24, 2018
Insights into IL-modified silica/6FDA-DAM ionic liquid mixed matrix membranes for CO2/CH4 separation: Integrated
Mehtab Ali Darban1, Serene Sow Mun Lock1, Abrar Ahmad1
1Centre for Sustainable Energy, Environment and Social Innovation (SEnSI), Universiti Teknologi PETRONAS, Seri Iskandar, 32610, Malaysia; Department of Chemical Engineering, Universiti Teknologi PETRONAS, Seri Iskandar, 32610, Malaysia.
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Mixed Matrix Membranes (MMMs) are considered a promising alternative to conventional natural gas sweetening processes. However, their performance is often hindered by poor filler dispersion and weak polymer-filler compatibility, which result in non-selective gas transport. Ionic liquids (ILs) can improve dispersion and enhance interfacial interactions, thereby improving separation performance, but identifying an appropriate polymer-filler-IL combination at the experimental scale is challenging due to the vast structural variations of ILs. This study introduces a novel integrated computational approach that combines quantum mechanics with atomistic computations to investigate IL-supported silica (IL-Si)/6FDA-DAM ILMMMs, aiming to establish a predictive mechanistic framework for the material formulation in CO2/CH4 separation. COSMO-RS was employed to screen 150 ILs using activity coefficient (γ) predictions, from which [P8888][Tf2N] was identified as the most CO2-philic candidate. This IL was then supported on silica and incorporated into a 6FDA-DAM matrix. The influence of IL-Si loading (0, 8, and 16 wt%) on thermophysical and transport properties was systematically examined under pure and mixed-gas environments (30, 50, and 70% CO2/CH4) at 35 °C and 1 atm, enabling molecular-level insight into the effect of gas composition on separation performance. Results showed that the glass transition temperature (Tg) of the hybrid membrane increased from 409 °C (neat 6FDA-DAM) to 421 °C at 8 wt% IL-Si, indicating strong filler dispersion and interfacial adhesion. For separation performance, the optimized membrane at 16 wt% IL-Si achieved a CO2 permeability of 1413.9 Barrer and a CO2/CH4 selectivity of 62.1 under 50 vol% CO2/CH4 conditions, corresponding to improvements of 114% in permeability and 193% in selectivity compared to neat 6FDA-DAM. The obtained results exhibited an error in the 0.7-9% range, confirming the reliability of the simulation framework. Overall, this study demonstrates the potential of simulation-driven design for tailoring IL-functionalized MMMs with enhanced stability, permeability, and selectivity for natural gas upgrading, while pointing toward future integration of molecular simulations with AI-based tools for accelerated discovery and optimization of next-generation membranes.
