Erkoç Ilter Selda
Integrated Manufacturing Technologies Research and Application Center & Composite Technologies Center of Excellence, Sabancı University, İstanbul, Turkiye.
Turk J Chem. 2025 Apr 25;49(4):404-418. doi: 10.55730/1300-0527.3740. eCollection 2025.
A synthesized zwitterionic monohydroxyl monomer (ZHM) was used as an additive to incorporate zwitterionic sulfobetaine groups into the polyamide (PA) active layers of thin-film composite membranes. Incorporation of ZHM into the PA active layers was achieved through interfacial polymerization, involving the introduction of ZHM and m-phenylenediamine (MPD) into the aqueous phase, and the addition of trimesoyl chloride (TMC) to the hexane phase. The surfaces of the resulting reverse osmosis (RO) membranes were subjected to characterization through water contact angle (WCA) and field emission scanning electron microscopy (FESEM) analyses. The successful incorporation of ZHM into the active PA layers was confirmed by X-ray photoelectron spectroscopy (XPS) and Fourier transform infrared spectroscopy (FTIR) analysis. To assess the flux and salt rejection performance of the fabricated membranes, aqueous solutions containing 2000 ppm NaCl or MgSO were filtered in a dead-end filtration system under a pressure of 15 bar. Compared to the control membrane (ZHM-0), the ZHM-modified membranes had significantly enhanced flux without compromising salt retention. In the NaCl solution filtration, the modified membrane (ZHM-1) increased in flux from 6.8 to 9.1 L/mh while having similar salt rejection (approximately 91%) in comparison to the control membrane (ZHM-0). In the MgSO solution filtration, the modified membranes increased in flux from 6.7 to 9.5 L/mh, while maintaining a consistent salt rejection rate of 100%, mirroring that of the control membrane.
一种合成的两性离子单羟基单体(ZHM)被用作添加剂,将两性离子磺基甜菜碱基团引入到薄膜复合膜的聚酰胺(PA)活性层中。通过界面聚合将ZHM引入PA活性层,这涉及将ZHM和间苯二胺(MPD)引入水相,并将均苯三甲酰氯(TMC)添加到己烷相中。通过水接触角(WCA)和场发射扫描电子显微镜(FESEM)分析对所得反渗透(RO)膜的表面进行表征。通过X射线光电子能谱(XPS)和傅里叶变换红外光谱(FTIR)分析证实了ZHM成功引入活性PA层。为了评估所制备膜的通量和脱盐性能,在15巴的压力下,在死端过滤系统中过滤含有2000 ppm NaCl或MgSO的水溶液。与对照膜(ZHM-0)相比,ZHM改性膜在不影响盐分保留的情况下通量显著提高。在NaCl溶液过滤中,改性膜(ZHM-1)的通量从6.8增加到9.1 L/mh,而与对照膜(ZHM-0)相比具有相似的脱盐率(约91%)。在MgSO溶液过滤中,改性膜的通量从6.7增加到9.5 L/mh,同时保持100%的一致脱盐率,与对照膜相同。