Nanoporous lyotropic liquid crystal polymer membranes with reversibly tuned pore size and selectivity, and methods using same
US-2018208728-A1 · Jul 26, 2018 · US
US11517860B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11517860-B2 |
| Application number | US-201916979030-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 8, 2019 |
| Priority date | Mar 8, 2018 |
| Publication date | Dec 6, 2022 |
| Grant date | Dec 6, 2022 |
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The invention relates to dense synthetic membranes made from polymerised phosphonium-based ionic liquids which were found to be particularly suitable for use in gas separation. The membranes are obtainable by copolymerization via UV-curing of a composition comprising a phosphonium-based ionic liquid monomer, a co-monomer, a cross-linker, a surfactant and a photo-initiator, the remainder of the polymerization mixture consisting of water.The invention also relates to a process of manufacturing said membranes, resulting in solid, dense and mechanically stable membranes, and to the use of the membranes so produced in the separation of gas mixtures, particularly gas mixtures containing carbon dioxide.
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The invention claimed is: 1. A dense poly(ionic liquid)-based membrane suitable for gas separation obtainable by copolymerization via UV-curing of a mixture comprising: a) 10 to 50 wt %, of a IL monomer trialkyl[(4-vinylphenyl)alkyl]phosphonium with X − as counterion ([TAVPAP]X) of the following formula: wherein each R represents an alkyl chain having 3 to 20 carbon atoms, L represents a linker consisting of a simple alkanediyl C 1 -C 20 chain, or an ethereal chain containing 1-20 carbon atoms and 1-10 oxygen atoms, and X − represents an anion selected from the group consisting of: BF 4 − , PF 6 − , SbF 6 − , TsO − , CF 3 —SO 3 − , NC—N − —CN, (MeO) 2 PO 2 − , EtSO 4 − or F 3 CO 2 SN − —SO 2 CF 3 b) 30 to 70% wt % of one or more ethylenically unsaturated co-monomers; c) 1 to 35 wt % of a surfactant; d) 0.5-20% wt %, of one or more cross-linkers, e) 0.001 to 5 wt % of a photo-initiator; f) the remainder of the mixture being water. 2. The dense poly(ionic liquid)-based membrane according to claim 1 , wherein each R represents an alkyl chain having 3 to 10 carbon atoms. 3. The dense poly(ionic liquid)-based membrane according to claim 2 , wherein each R represents butyl, hexyl or octyl. 4. The dense poly(ionic liquid)-based membrane according to claim 1 , wherein L represents a methanediyl group. 5. The dense poly(ionic liquid)-based membrane according to claim 1 , wherein the ethylenically unsaturated co-monomer is 2-hydroxyethyl acrylate (HEMA), and is present in the composition in the amount of 50-60 wt %. 6. The dense poly(ionic liquid)-based membrane according to claim 5 , wherein the IL monomer is present in the composition at a concentration of 20-30 wt %, the surfactant is present at a concentration of 10-30 wt %, the cross-linker is present at a concentration of 1-10 wt % and the photo-initiator is present at a concentration of 0.1 to 1 wt %. 7. A process for producing dense poly(ionic liquid) membranes suitable for gas separation, which process includes the following steps: providing a mixture as defined under items a) to f) of claim 1 ; applying said mixture to a support by means of a film casting knife or casting said mixture between two plates so that the thickness of the membrane ranges between 0.02 and 200 μm; curing said curable monomer mixture by UV radiation to induce polymerization. 8. A method of gas separation comprising using a membrane according to claim 1 . 9. Use according to claim 8 wherein said gases to be separated include carbon dioxide (CO 2 ), hydrogen (H 2 ), methane (CH 4 ), nitrogen (N 2 ) and oxygen (O 2 ). 10. A process for separating two components, A and B, of a gas mixture, which process comprises: i. passing said gas mixture across a separation membrane having a feed side and a permeate side, said separation membrane having a selective layer produced as defined in claim 7 ; ii. providing a driving force for transmembrane permeation; iii. withdrawing from the permeate side a permeate stream enriched in component A compared to the gas mixture; and iv. withdrawing from the feed side a residue stream depleted in component A compared to the gas mixture. 11. A method of gas separation comprising using a membrane produced according to the process of claim 7 . 12. The dense poly(ionic liquid)-based membrane according to claim 1 , wherein the IL monomer trialkyl[(4-vinylphenyl)alkyl]phosphonium is present in the composition in the amount of 20-30 wt %. 13. The dense poly(ionic liquid)-based membrane according to claim 1 , wherein the one or more ethylenically unsaturated co-monomers is present in the composition in the amount of 50-60 wt %. 14. The dense poly(ionic liquid)-based membrane according to claim 1 , wherein the one or more ethylenically unsaturated co-monomers comprises acrylates. 15. The dense poly(ionic liquid)-based membrane according to claim 1 , wherein the surfactant is present in the composition in the amount of 10-30 wt %. 16. The dense poly(ionic liquid)-based membrane according to claim 1 , wherein the one or more cross-linkers is present in the composition in the amount of 2-10 wt %. 17. The dense poly(ionic liquid)-based membrane according to claim 1 , wherein the photo-initiator is present in the composition in the amount of 0.1-1 wt %.
Oxygen · CPC title
by chemical reactions (in-situ polymerisation, polycondensation, cross-linking or reaction for manufacturing composite membranes B01D69/125) · CPC title
Nitrogen · CPC title
Carbon dioxide · CPC title
in-situ membrane formation · CPC title
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