CO2-Philic [EMIM][Tf2N] modified silica in mixed matrix membrane for high performance CO2/CH4 separation

Separation of carbon dioxide (CO 2 ) from methane (CH 4 ) using polymeric membranes is limited by trade-off between permeability and selectivity as depicted in Robeson curve. To overcome this challenge, this study develops membranes by incorporating silica particles (Si) modified with [EMIM][Tf 2 N]...

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Bibliographic Details
Main Authors: Siti Nur Alwani, Shafie, Wen, Xuan Liew, Nik Abdul Hadi, Md Nordin, Bilad, Muhammad Roil, Norazlianie, Sazali, Zulfan, Adi Putra, Mohd Dzul Hakim, Wirzal
Format: Article
Language:English
Published: Wiley 2019
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Online Access:http://umpir.ump.edu.my/id/eprint/25529/
http://umpir.ump.edu.my/id/eprint/25529/
http://umpir.ump.edu.my/id/eprint/25529/
http://umpir.ump.edu.my/id/eprint/25529/1/CO_2_-Philic_EMIMTf_2_N_Modified_Silica_in_Mixed_M.pdf
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Summary:Separation of carbon dioxide (CO 2 ) from methane (CH 4 ) using polymeric membranes is limited by trade-off between permeability and selectivity as depicted in Robeson curve. To overcome this challenge, this study develops membranes by incorporating silica particles (Si) modified with [EMIM][Tf 2 N] ionic liquid (IL) at different IL:Si ratio to achieve desirable membrane properties and gas separation performance. Results show that the IL:Si particle has been successfully prepared, indicated by the presence of fluorine and nitrogen elements, as observed via Fourier-Transform Infrared Spectroscopy (FTIR) and X-ray Photoelectron Spectrometer (XPS). Incorporation of the modified particles into membrane has given prominent effects on morphology and polymer chain flexibility. The mixed matrix membrane (MMM) cross-section morphology turns rougher in the presence of IL:Si during fracture due to higher loadings of silica particles and IL. Furthermore, the MMM becomes more flexible with IL presence due to IL-induced plasticization, independent of IL:Si ratio. The MMM with low IL content possesses CO 2 permeance of 34.60 ± 0.26 GPU with CO 2 /CH 4 selectivity of 85.10, which is far superior to a pure polycarbonate (PC) and PC-Sil membranes at 2 bar, which surpasses the Robeson Upper Bound. This higher CO 2 selectivity is due to the presences of CO 2 -philic IL within the MMM system.