新型ɑ-纤维素/聚砜共混超滤膜的制备与性能研究
作者:郑虹12  介兴明1  于海军1 李霞12    况武12  陈勇3 曹义鸣
单位: 1. 中国科学院大连化学物理研究所,大连116023; 2. 中国科学院大学,北京100049;3.辽宁华孚环境工程股份有限公司,124013
关键词: ɑ-纤维素;NMMO?H2O;共混;超滤;亲水改性
DOI号:
分类号: 0631;TQ028.8
出版年,卷(期):页码: 2015,35(6):1-8

摘要:
 以聚砜为原材料,在铸膜液中添加ɑ-纤维素,采用浸没沉淀法制备了新型ɑ-纤维素/聚砜共混超滤膜.主要考察了溶剂因素对共混膜的制备及渗透性能的影响.实验发现:N,N-二甲基乙酰胺(DMAC),N-甲基吡咯烷酮(NMP),NMP与N-甲基吗啉N-氧化物水合物(NMMO•H2O)混合溶剂均可用于制备共混膜;红外光谱(FTIR)、热重(TG)、差式扫描量热法(DSC)和扫描电子显微镜(SEM)表征表明NMMO•H2O+NMP混合溶剂所制得的膜聚合物共混均匀,膜表面较为光滑,无明显缺陷,是α-纤维素和聚砜共混铸膜体系的良溶剂;膜性能测试结果表明加入α-纤维素的共混膜亲水性得到明显改善,水接触角由72º降低为51º,纯水通量和牛血清蛋白(BSA)溶液通量分别为443.40L/m2•h和147.65L/m2•h,比纯聚砜膜增加约2.6倍和1.7倍,同时对BSA的截留率保持在95%以上.膜抗污染能力测试[将此处改为“能量恢复情况”,并且请全文统一。另外终审专家提出:能量恢复情况和污染阻力是否可以完全证明抗污染性能的提高,请统一说法]结果表明以混合溶剂制备的分离膜水洗后通量恢复率较高,污染阻力小,抗污染性能提高明显。
 
 A novel blend membrane prepared by ɑ- cellulose and polysulfone(PSF) using immersion-precipitation process. This paper mainly studied the influence of solvent system on the preparation process and filtration performance of blend membrane. It was found that only three solvents: N,N-dimethyl-Acetamide(DMAC)、 N-methyl pyrrolidone(NMP)、 N-methyl pyrrolidone(NMP) and N- methylmorpholine N-oxide hydrate(NMMO•H2O)can be used to prepare blend membranes successfully. Among them, NMMO•H2O+NMP has been proved to be the best solvent. The membranes were characterized by Fourier transform infrared spectroscopy (FTIR), thermogravimetry(TG), Differential scanning calorimetry (DSC) and scanning electron microscopy(SEM). It has been confirmed that cellulose in the casting solution dissolved by NMMO•H2O+NMP was better-distributed, and its surface was smoother without any significant defect than the blend membranes prepared by other solvents. The tests of contact angle (CA), water flux and fluid of Bovine serum albumin (BSA) flux indicated that the hydrophilicity of PSF membrane has been obviously improved by blending α-cellulose. With NMMO•H2O+NMP as solvent the CA has been lowered from 72º to 51º; the water flux was improved to about 443.40L/m2•h, which is 2.6 folds higher than PSF membrane (121.95L/m2•h); and at the same time the BSA fluid flux has been increased 1.7 folds compared with the original PSF membrane. What is more, the rejection rate still maintained above 95%. With an anti-fouling test, the membrane prepared by NMMO•H2O+NMP showed a higher flux recovery rate, which means it has a better hydrophicility and owns broader application prospect. 
 

基金项目:
国家自然科学基金(批准号:21206157)和国家科技支撑计划项目(批准号:2014BAI11B13)资助.

作者简介:
郑虹(1990一 ),女,陕西省咸阳市人,硕士生,从事分离膜的开发和应用.

参考文献:
 1Zhang G, Lu S, Zhang L, et al. Novel polysulfone hybrid ultrafiltration membrane prepared with TiO2-g-HEMA and its antifouling characteristics[J]. J Membr Sci,2013,436:163-173
2Kumari A, Sarkhel G, Choudhury A. Effect of Polyvinylpyrrolidone on Separation Performance of Cellulose Acetate-Polysulfone Blend Membranes[J], Journal of Macromolecular Science, Part A, 2013,50:692-702
3Dos Santos T, Pacheco KA, Poletto P, et al. Effect of cellulose fibers on morphology and pure water permeation of PSf membranes[J]. Desalination and Water Treatment ,2011,27:72-75
4Schmidtsteffen A, Staude E. Ultrafiltration membranes for chemical bonding of urease[J], Biotechnol Bioeng, 1992,39:725-31
5Sivakumar M, Mohan DR, Rangarajan R. Studies on cellulose acetate-polysulfone ultrafiltration membranes, Journal of Membrane Science[J], 2006,268:208-19
6Bhat KA,Rajangam P, Dharmalingam S. Fabrication and characterization of polymethylmethacrylate /polysulphone/beta-tricalcium phosphate composite for orthopaedic applications[J]. J Mater Sci, 2012,47:1038-1045
7Bowen WR, Doneva TA, Yin HB. Separation of humic acid from a model surface water with PSU/SPEEK blend UF/NF membranes[J]. J Membr Sci, 2002,206:417-429
8Eren E, Sarihan A, Eren B, et al. Preparation, characterization and performance enhancement of polysulfone ultrafiltration membrane using PBI as hydrophilic modifier [J].J Membr Sci,2015,475: 1-8
9Zularisam AW, Ismail AF, Salim MR, et al. The effects of natural organic matter (NOM) fractions on fouling characteristics and flux recovery of ultrafiltration membranes[J]. Desalination, 2007,212:191-208
10张耀鹏,邵惠丽,沈新元,等.NMMO法纤维素膜的结构与性能[J].膜科学与技术,2002,22(4):13 -20
11张力平,陈国伟,唐焕威,等.聚砜- 纤维素复合超滤膜材料的制备与表征[J].生物质化学工程,2008,42(2):11-16
12介兴明,曹义鸣,李红剑,等.纤维素直接溶解成膜及其分离特性研究进展[J].化工学报,2006,57(8):1756-1762
13Fink HP, Ganster J, Lehmann A. Progress in cellulose shaping: 20 years industrial case studies at Fraunhofer IAP [J].Cellulose, 2014,21(1):31-51
14Wu J, Yuan Q. Gas permeability of a novel cellulose membrane[J]. J Membr Sci, 2002;204:185-194
15Jie XM, Cao YM, Lin B, et al. Gas permeation performance of cellulose hollow fiber membranes made from the cellulose/N-methylmorpholine-N-oxide/H2O system[J], J Appl Polym Sci, 2004;91:1873-1880
16Li HH, Cao YM, Qin HJ,et al. Development and characterization of anti-fouling cellulose hollow fiber UF membranes for oil-water separation[J]. J Membr Sci, 2006;279:328-335
17Yong-Ming Wei, Zhen-Liang Xu, Xiao-Tian Yang, et al. Mathematical calculation of binodal curves of a polymer/solvent/nonsolvent system in the phase inversion process[J]. Desalination,2006;192: 91–104
18秦建军,江成璋.聚砜制膜液体系的相图研究[J].膜科学与技术,1990,10(3):13-18
19Ishii D, Tatsumi D, Matsumoto T. Effect of solvent exchange on the solid structure and dissolution behavior of cellulose[J]. Biomacromolecules,2003,4(5): 1238-1243
20Yang Yun-Feng, Wang Ling-Shu, Xu Zhi-Kang. Surface hydrophilization of microporous polypropylene membrane by the interfacial crosslinking of polyethylenimine[J]. J Membr Sci,2009,326(2):372-381
21徐辉.膜生物反应器处理生活污水研究[D].吉林:吉林大学,2005.

服务与反馈:
文章下载】【加入收藏

《膜科学与技术》编辑部 地址:北京市朝阳区北三环东路19号蓝星大厦 邮政编码:100029 电话:010-64426130/64433466 传真:010-80485372邮箱:mkxyjs@163.com

京公网安备11011302000819号