Novel membrane shows improved ion exchange capacity and stability in mixed cation systems, indicating potential for advanced separation processes.
Monovalent cation exchange membranes (MCEMs) are central to selectrodialysis (SED), which enables precise ion fractionation. In this study, a novel type of MCEMs were designed for the separation of mixed acid/salt systems via SED. The membranes were fabricated by first doping Ti3C2TX nanosheets into a sulfonated polysulfone (SPPSU) matrix, followed by spray-coating quaternized poly(2,6-dimethyl-1,4-phenylene oxide) (QPPO) layers synthesized from brominated polyphenylene oxide and tertiary amines with varying alkyl chain lengths. The incorporation of 0.5 wt % Ti3C2TX into SPPSU (yielding the SPPSU-T membrane) enhanced the ion exchange capacity by 1.10-fold (to 1.53 mmol·g–1) and water uptake by 1.01-fold (to 16.10%) relative to the pristine SPPSU membrane, resulting in a reduced area resistance (2.08 vs 2.14 Ω·cm–2) and a 1.30-fold increase in H+ flux (7.31 × 10–8 mol·cm–2·s–1). Although the optimized SPPSU-T-QPPO18-1.02 (coated with 1.02 g·m–2 of QPPO quaternized with N,N-dimethyldodecylamine) exhibited a 3.11-fold increase in area resistance compared to the pristine SPPSU-T membrane, it had a 12.32-fold higher H+/Mg2+ selectivity (PMgH = 87.59). Moreover, the SPPSU-T-QPPO18-1.02 also achieved 14.23-fold and 5.13-fold higher selectivity for H+ over Zn2+ (PZnH = 29.32) and Fe2+ (PFeH = 9.149), respectively, compared to SPPSU (PZnH = 2.06, PFeH = 1.78). In the three investigated acid/salt systems, the SPPSU-T-QPPO18-1.02 delivered competitive H+ flux (6.97∼8.78 × 10–8 mol·cm–2·s–1) and selectivity (9.14∼87.59) compared to the commercial CIMS membrane (flux: 6.00∼8.68 × 10–8 mol·cm–2·s–1; selectivity: 1.98∼4.11). Furthermore, it demonstrated excellent long-term operational stability in SED processing of MgCl2/HCl mixtures. This work demonstrates that incorporating Ti3C2TX nanosheets into the membrane matrix and coating with a tailored QPPO layer can synergistically overcome the trade-off between ion flux and selectivity in MCEMs, providing an effective strategy for advanced membrane design.
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Liu et al. (2026) studied this question.
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