氟化聚醚砜疏水膜的制备及其膜蒸馏应用
作者:刘丽霞12,沈飞2,罗建泉2,万印华2
单位: 1.化学化工学院,聊城大学,山东聊城,252300; 2.生化工程国家重点实验室,中国科学院过程工程研究所,中国科学院大学,北京 100190
关键词: 膜蒸馏 聚醚砜 辐照接枝 反渗透浓水 脱盐
出版年,卷(期):页码: 2021,41(4):93-101

摘要:
 以全氟辛基乙基甲基丙烯酸酯(FMA-C8)为接枝单体,采用溶液均相共辐照方式(60Co γ 射线)对聚醚砜(PES)材料进行疏水改性,制备得到氟化的PES(PES-g-PFMA-C8),进而将其喷涂在自制多孔PES膜表面制备得到疏水化的PES膜。借助红外光谱、光电子能谱、接触角仪等对PES-g-PFMA-C8及其改性膜进行表征,探究喷涂疏水改性对PES膜性能的影响。结果表明,疏水改性的PES膜(H-PES膜)的疏水性较PES膜显著提高,接触角由73.1 °增大到109.3 °,液体进入压力由295 kPa提高到410 kPa,70 °C下对3.5 wt% NaCl盐溶液进行真空膜蒸馏时,80 h长时间运行过程中通量保持在50 kg m-2 h-1左右,脱盐率高达99.98%;且该膜应用于海水淡化反渗透浓水处理过程中,产水水质稳定,能将海水淡化的总体水回收率由45%提高到83.7%,在膜蒸馏脱盐方面具有较好的应用潜力。
 1H, 1H, 2H, 2H-perfluorodecyl methacrylate (FMA-C8) was used as monomer, and grafted onto polyethersulfone (PES) by simultaneous irradiation in a homogeneous system under 60Co γ ray. The grafted product PES-g-PFMA-C8 with high hydrophobicity was obtained. PES-g-PFMA-C8 was then sprayed onto home-made porous PES membranes to fabricate hydrophobic PES membranes (H-PES). The effects of spraying on PES membranes were investigated via Fourier transformed infrared spectroscopy, X-ray photo electronic spectroscopy and optical contact angle goniometer, etc. The results showed that the hydrophobicity of H-PES membrane increased obvisouly after spraying modification: contact angle increased from 73.1 ° to 109.3 °, and liquid entry pressure increased from 295 kPa to 410 kPa. During an intermittent 80 h VMD desalination operation, a flux of approximately 50 kg m-2 h-1 and a stable salt rejection of 99.98% were achieved when a 3.5 wt% NaCl solution was treated at 70 °C by the H-PES membrane. Furthermore, the H-PES membrane was applied to concentrate RO brines, and the permeate quality was high, and the water recovery increased from 45% to 83.7%, showing great potential in the real application of membrane distillation desalination. 
刘丽霞(1988-),女,山东聊城人,讲师,博士,从事膜材料改性和膜制备研究

参考文献:
 [1] Yan H, Lu X, Wu C, et al. Fabrication of a super-hydrophobic polyvinylidene fluoride hollow fiber membrane using a particle coating process[J]. J Membr Sci, 2017, 533: 130-140.
[2] Xie B, Xu G, Jia Y, et al. Engineering carbon nanotubes enhanced hydrophobic membranes with high performance in membrane distillation by spray coating[J]. J Membr Sci, 2020: 118978.
[3] Khalifa A, Ahmad H, Antar M, et al. Experimental and theoretical investigations on water desalination using direct contact membrane distillation[J]. Desalination, 2017, 404: 22-34.
[4]  唐敏, 贾晓琳, 张勇, 等. 新型 Janus 膜的制备及其在高盐含油废水膜蒸馏处理中的应用[J]. 环境工程学报, 2020, 14(8):
2037-2047.
[5] 曾崇阳, 锐谢, 巨晓洁, 等. 共混改性法制备高性能聚砜温敏膜[J]. 膜科学与技术, 2020, 40(6): 14-21.
[6]   Khana A, Siyala M, Lee C, et al. Hybrid organic-inorganic functionalized polyethersulfone membrane for hyper-saline feed with humic acid in direct contact membrane distillation[J]. Sep Purif Technol, 2019, 210: 20–28.
[7] Suk D, Matsuura T, Park H, et al. Development of novel surface modified phase inversion membranes having hydrophobic surface-modifying macromolecule (nSMM) for vacuum membrane distillation[J]. Desalination, 2010, 261(3): 300-312.
[8] Wei X, Zhao B, Li X, et al. CF4 plasma surface modification of asymmetric hydrophilic polyethersulfone membranes for direct contact membrane distillation[J]. J Membr Sci, 2012, 407-408: 164-175.
[9] Mazzei R, Smolko E, Tadey D, et al. Radiation grafting of NIPAAm on PVDF nuclear track membranes[J]. Nucl Instrum Meth B, 2000, 170(3-4): 419–426.
[10] Yang X, Deng B, Liu Z, et al. Microfiltration membranes prepared from acryl amide grafted poly(vinylidene fluoride) powder and their pH sensitive behaviour[J]. J Membr Sci, 2010, 362: 298-305.
[11] Deng B, Yang X, Xie L, et al. Microfiltration membranes with pH dependent property prepared from poly(methacrylic acid) grafted polyethersulfone powder[J]. J Membr Sci,  2009, 330(1-2): 363-368.
[12] Geng W, Nakajima T, Takanashi H, et al. Determination of total fluorine in coal by use of oxygen flask combustion method with catalyst[J]. Fuel, 2007, 86(5-6): 715-721.
[13]  Xu K, Cai Y, Hassankiadeh N, et al. ECTFE membrane fabrication via TIPS method using ATBC diluent for vacuum membrane distillation[J]. Desalination, 2019, 456: 13-22. 
[14] Song Z, Tang J, Li J, et al. Plasma-induced polymerization for enhancing paper hydrophobicity[J]. Carbohyd Polym, 2013, 92(1): 928-933.
[15] Kaeselev B, Kingshott P, Jonsson G. Influence of the surface structure on the filtration UV-modified PES membranes [J]. Desalination, 2002, 146: 265-271 
[16] 周晓吉, 黄晶, 张迪, 等. 两性离子聚合物共混改性聚偏氟乙烯膜性能研究[J]. 水处理技术, 2020, 46(3): 80-85.
[17] Shan H, Liu J, Li X, et al. Nanocoated amphiphobic membrane for flux enhancement and comprehensive anti-fouling performance in direct contact membrane distillation[J]. J Membr Sci,  2018, 567: 166-180.
[18] Gryta M. Long-term performance of membrane distillation process[J]. J Membr Sci, 2005, 265(1-2): 153-159.
[19] 秦英杰, 刘立强, 何 菲, 等. 内部热能回收式多效膜蒸馏用于海水淡化及浓盐水深度浓缩[J]. 膜科学与技术, 2012, 32(2): 52-58.
[20] Sanmartino J, Khayet M, García-Payo M, et al. Desalination and concentration of saline aqueous solutions up to supersaturation by air gap membrane distillation and crystallization fouling[J]. Desalination, 2016, 393: 39-51.
[21] Guillen-Burrieza E, Thomas R, Mansoor B, et al. Effect of dryout on the fouling of PVDF and PTFE membranes under conditions simulating intermittent seawater membrane distillation (SWMD)[J]. J Membr Sci, 2013, 438: 126-139.
[22] 侯得印, 王军, 王宝强, 等. PVDF 疏水膜的制备及其在苦咸水脱盐中的应用[J]. 北京大学学报(自然科学版), 2010, 46(3): 395-400.
[23] Zhao S, Hu S, Zhang X, et al. Integrated membrane system without adding chemicals for produced water desalination towards zero liquid discharge[J]. Desalination, 2020, 496: 114693
[24] 张新妙, 赵 鹏, 杨永强, 等, 膜蒸馏技术用于高盐污水回用研究[J]. 现代化工, 2012, 32(6): 83-88.

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