耐溶剂聚酰亚胺纳滤膜的制备与分离性能

本文以均苯四甲酸二酐(PMDA)和4,4′ 二氨基二苯醚(ODA)为原料,采用相转化法制备了耐溶剂的聚酰亚胺(PI)纳滤膜。通过对原料进行预处理,调节反应时间,使得聚酰胺酸(PA)特性粘度稳定在0 99mL g。试验结果表明,当聚酰胺酸铸膜液质量分数为15%,溶剂挥发时间为30min,凝胶浴为乙醇质量分数30%的乙醇 水溶液时,所制得的聚酰亚胺纳滤膜具有最佳的分离性能。操作压力为2MPa时,该膜对聚乙二醇300(PEG300)水溶液截留率可达91%,通量为5 75L (m2·h)。为进一步研究适用于有机溶剂体系的纳滤膜技术提供了基础。     

芳香聚酰胺纳滤膜的制备及性能研究

以芳香聚酰胺为原料,采用相转化法制备了芳香聚酰胺纳滤膜,通过正交试验确定了最佳制膜工艺.详细讨论了纳滤膜的分离特性,并对纳滤膜的耐溶剂及抗污染性能进行了初步研究.实验结果表明,所制芳香聚酰胺纳滤膜对无机盐及小分子有机物具有较好的选择分离性能.操作压力为0.4MPa时,该膜对蔗糖的截留率为63.74%,对葡萄糖的截留率为54.36%.膜具有很好的耐溶剂性和抗污染性.     

N,O-羧甲基壳聚糖/聚砜复合纳滤膜的制备及性能研究

以聚砜(PsF)超滤膜为基膜、N,O-羧甲基壳聚糖(NOCC)水溶液为活性层铸膜液、戊二醛(GA)为交联剂,采用涂敷和交联的方法制备了复合纳滤膜.测试了膜表面的流动电势(E)随操作压力(△P)的变化,实验结果表明在电解质溶液中,NOCC/PSF复合NF膜表面荷负电.对其结构和形貌进行了表征,并研究了有机小分子添加剂对复合膜截留性能的影响.NOCC/PSF复合NF膜对几种无机盐的截留顺序为Na2S04＞NaCl＞MgSOa＞MgCl2,呈现出荷负电纳滤膜的截留特征.     

对硝基苯酚复合纳滤膜的制备及性能研究

采用PNP作为膜材料制备耐溶剂复合纳滤膜,采用界面聚合反应法制备了一种有机溶剂纳滤膜.在N,N-二甲基甲酰胺(DMF)中,PNP和三甲基氯(TMC)在聚酯键结构上具有稳定的耐溶剂性.NF-1PNP膜保持稳定的DMF性能.在连续分离36 h的条件下,对孟加拉红(RB 1017.64 g·mol-1)的吸附通量为21 L·...     

基于MXene中间层的复合纳滤膜制备及其盐水分离性能研究

通过湿法化学刻蚀得到单层MXene纳米片后,采用旋涂法将MXene纳米片负载至基膜上作为中间层制备聚酰胺复合纳滤膜,并探讨了MXene不同负载浓度对复合纳滤膜通量及盐截留性能的影响。结果表明引入MXene作为中间层,使得圆泡状形貌在所得膜表面形成,当旋涂1 mL浓度为0.1 g/L MXene时,通量为24.2 L/(m²·h),硫酸钠截留率为97.4%,相比传统膜(通量12.9 L/(m²·h),硫酸钠截留率96.3%)性能提升明显。随着MXene旋涂负载浓度增加,通量逐渐减小,而硫酸钠截留率则存在先增加后减小再稳定的趋势,截留率最高可达98.8%(通量16.3 L/(m²·h))。     

聚乙烯醇复合纳滤膜的性能研究

本文采用涂敷法制得聚乙烯醇 (PVA)复合纳滤膜 ,并对膜的分离性能、耐溶剂性、耐压密性进行了测试。结果表明 :该复合纳滤膜在 0 .6MPa操作压力下水通量为 12L·m-2 ·h-1,对 5 0 0mg/L的标准物质PEG6 0 0的截留率达到 90 .8% ,并随着操作压力的增加 ,水通量呈线性增加 ,截留率也相应上升 ,该膜具有较好的耐压密性 ,耐酸碱性和耐氧化性 ,并通过红外光谱分析复合纳滤膜致密层的化学结构     

一种新型共混复合纳滤膜的制备及性能研究

以海藻酸钠(ALG)和羧甲基纤维素钠(CMC)共混液为活性层铸膜液,聚砜(PSF)超滤膜为基膜,环氧氯丙烷(ECH)的乙醇溶液为交联剂,采用涂敷和交联的方法制得一种新型复合纳滤膜,利用红外光谱仪、扫描电子显微镜、原子力显微镜和接触角测量仪等检测手段对复合膜进行了结构和性能的表征。结果表明,在1.0 MPa压力和30 L?h-1料液流量操作条件下,该复合纳滤膜对1000 mg?L-1 Na2SO4溶液的截留率为97.1%,通量17.3 L?m-2?h-1。以ALG和CMC共混液制备的复合纳滤膜比单一材料膜有更致密的膜面结构,截留率更高。该纳滤膜对不同无机盐的截留性能不同,表现出荷负电膜截留性能,这主要决定于荷电膜与电解质离子之间的静电作用力。     

聚哌嗪酰胺复合纳滤膜的制备及表征

用哌嗪(PIP)溶液为水相反应单体,均苯三甲酰氯(TMC)正庚烷溶液为有机相反应单体,通过界面聚合法制备聚哌嗪酰胺中空纤维复合纳滤膜,研究了水相单体和有机相单体浓度对纳滤膜的影响及基膜预处理、对复合纳滤膜进行后处理对复合纳滤膜分离性能的影响,采用扫描电镜(SEM)和原子力显微镜(AMF)对制备的纳滤膜进行表征,所制备的聚酰胺复合纳滤膜在操作压力0.6 MPa下,对质量浓度2 000 mg/L的MgSO4溶液的脱除率为90%以上。     

磺化TA/CS复合纳滤膜的制备及性能研究

利用Fe~(3+)的配位作用使单宁酸(TA)/壳聚糖(CS)胶体粒子在改性聚丙烯腈(PAN)超滤膜的表层快速共沉积,然后在其表面上与均苯三甲酰氯(TMC)进行界面聚合,制备了复合纳滤膜。在水相中添加2,4-二氨基苯磺酸(2,4-DABSA),考察引入磺酸基团后复合膜的过滤及抗污染性能。结果表明,磺化TA/CS复合膜对Na_2SO_4和MgSO_4的截留率分别达到96.21%和90.35%,并且在0.1 g/L腐殖酸、牛血清白蛋白环境下过滤24 h后均具有优异的通量恢复率。     

羧甲基纤维素钠复合纳滤膜的制备与性能表征

以羧甲基纤维素钠(CMC)为活性层铸膜液,聚砜(PSF)超滤膜为基膜,戊二醛(GA)水溶液为交联剂,采用涂敷和交联的方法制得一种新型荷负电复合纳滤(NF)膜。测定了复合膜的截留相对分子质量,并对其表面形貌进行了表征。在铸膜液中添加质量分数为3.5%的不同种类有机小分子,研究了其对复合膜截留性能的影响。CMC/PSF复合膜对几种无机盐的截留顺序为:Na2SO4>NaCl>MgSO4>MgCl2。     

Investigation on the enhancement of solvent-resistant nanofiltration membrane performance utilizing PDA-UiO-66@CNT as an interlayer

With the growing complexity of separation systems, the application of thin film composite nanofiltration (TFN) membranes in organic solvent separation faces numerous challenges. To augment its solvent stability, an in-situ constructed dopamine hydrogel doped with UiO-66@CNT was developed as an intermediate layer on a polyetherimide (PEI) ultrafiltration membrane. Subsequent interfacial polymerization on this interlayer led to the formation of a solvent-resistant nanofiltration membrane with a vast covalent bond structure, large specific surface area, and enhanced hydrophilicity. Our findings revealed that when the CNT loading in the UiO-66@CNT composite nanoparticles was 2 wt%, the TFN-U₂C₂ membrane exhibited a maximum pure water flux of 126.32 L/(m²·h) and a methanol flux of 45.45 L/(m²·h). The rejection rates for Congo red aqueous and methanol solutions were 96.88% and 92.14%, respectively. The membrane also demonstrated commendable anti-fouling properties. Remarkably, even after 48 h of immersion in various organic solvents, the membrane retained its morphology and separation efficiency. Compared to the TFN-U₂ membrane without CNT addition, the enhancement in separation performance was considerably significant. Hence, this membrane has significant potential for application in treatment of wastewater containing organic solvents and is promising in related fields.     

Flow synthesis of a novel zirconium-based UiO-66 nanofiltration membrane and its performance in the removal of p-nitrophenol from water

In this work, a thin zirconium-based UiO-66 membrane was successfully prepared on an alumina hollow fiber tube by flow synthesis, and was used in an attempt to remove p-nitrophenol from water through a nanofiltration process. Two main factors, including flow rate and synthesis time, were investigated to optimize the conditions for membrane growth. Under optimal synthesis conditions, a thin UiO-66 membrane of approximately 2 µm in thickness was fabricated at a flow rate of 4 mL·h⁻¹ for 30 h. The p-nitrophenol rejection rate for the as-prepared UiO-66 membrane applied in the removal of p-nitrophenol from water was only 78.1% due to the existence of membrane defects caused by coordinative defects during membrane formation. Post-synthetic modification of the UiO-66 membrane was carried out using organic linkers with the same flow approach to further improve the nanofiltration performance. The result showed that the p-nitrophenol rejection for the post-modified membrane was greatly improved and reached over 95%. Moreover, the post-modified UiO-66 membrane exhibited remarkable long-term operational stability, which is vital for practical application.     

Preparation and separation properties of polyamide nanofiltration membrane

Utilizing an interfacial polymerization technique for the preparation of a polymeric composite nanofiltration membrane, both high permeation flux of water and high salt rejection can be achieved. Synthesis conditions, such as concentration of monomer, reaction time, and swelling agent, significantly affected the separation performance of composite membranes. The composite polyamide membrane had a permeation rate of ～2–5 gallon/ft²/day (gfd) and a salt rejection rate of ～94–99% when 2000 ppm aqueous salt solution was fed at 200 psi and 25°C. Also, a higher performance nanofiltration membrane could be prepared by suitably swelling the support matrix in the period of polymerization. The results of various feed concentrations showed that permeate flux decreased with increasing salt concentration in the feed solution. This result may be due to concentration polarization on the surface of polyamide membranes. The separation performance of polyamide membranes showed an almost independent relationship with operation pressure until it was up to 200 psi. © 2002 Wiley Periodicals, Inc. J Appl Polym Sci 83: 1112–1118, 2002     

耐溶剂复合纳滤膜的研究进展

耐溶剂纳滤是一种新型的膜分离技术,用于有机混合物的分离。商品耐溶剂纳滤膜大多是采用相转化法制备的整体皮层非对称膜,膜皮层较厚,通量较低。耐溶剂复合纳滤膜由基膜和分离层组成,具有薄皮层、高溶剂通量和高溶质截留率的优点。耐溶剂复合纳滤膜的制备与改性也因此成为近年来的研究热点。本文从界面聚合、表面涂覆、层层自组装、原位生长、有机-无机杂化和表面改性六个方面介绍耐溶剂复合纳滤膜的研究进展,最后对其发展前景进行展望。     

Preparation and performance of novel thermal stable composite nanofiltration membrane

The novel thermal stable composite nanofiltration membranes were prepared through the interfacial polymerization of piperazine and trimesoyl chloride on the poly (phthalazinone ether) ultrafiltration substrate. The effects of polymerization and testing conditions on membrane performance were studied. The surface morphologies of the substrate and the composite membranes were observed by means of scanning electron microscopy (SEM) and atomic force microscopy (AFM). The separation properties of membranes for dyes and salts were tested. The composite membranes show good thermal stability. The rejection for Na2SO4 was kept over 96%, while the flux reached 400 L·m⁻²·h⁻¹ when it was tested at 1.0 MPa and 80°C. When tested at 1.0 MPa and 60°C, the rejection of the composite membrane for dyes was kept at high level, and the flux reached 180–210 L·m⁻²·h⁻¹, while the rejection for NaCl was lower than 20%. __________ Translated from the Journal of Functional Materials, 2007, 38(12): 2025–2027, 2031 [译自: 功能材料]     

界面聚合法PI/PP耐溶剂复合纳滤膜的制备与表征

以丙烯酰胺接枝的聚丙烯(PP)超滤膜为支撑层,间苯二胺(MPD)、均苯四甲酰氯(BTAC)分别为水相及有机相功能单体,通过界面聚合及其后续的酰亚胺化制备了聚酰亚胺(PI)/PP耐溶剂复合纳滤膜。讨论了水相浓度、有机相浓度及酰亚胺化溶液配方等条件对复合膜结构及其分离性能的影响。分别采用傅里叶红外光谱仪(FTIR)、扫描电子显微镜(SEM)表征分离层的化学组成及复合膜的形态结构,得到膜的分离、透过及其耐溶剂性能。结果表明,有机相浓度的影响最为显著,支撑膜表面形成了均匀致密的PI分离层,复合膜呈负电性,并具备优秀的耐溶剂性能。实验范围内,MPD、BTAC的浓度分别为8、2 g·L-1,酰亚胺化溶液乙酸酐∶三乙胺∶苯体积比为1∶1∶10时,所制备膜的分离性能较佳,对Na2SO4、酸性艳蓝6B的截留率分别达93.8%和96.9%。     

新型复合纳滤膜研究进展

纳滤膜因操作压力低、通量高、具有分离选择性以及运行成本较低等优势引起越来越多的关注,目前已在苦咸水脱盐、污水治理和海水淡化等领域发挥着重要作用。界面聚合作为常见的制备聚酰胺纳滤膜的方法,其聚合反应进程的调控可以有效地调节纳滤膜的微观结构,进而对其分离性能产生重要影响。本文从复合纳滤膜的结构入手,总结了当前常用的提升纳滤膜性能的改性方法,包括优化分离选择层、构建中间层、调整底膜结构三个方面,讨论了界面聚合过程反应单体、添加剂种类、制备条件等对分离层结构和分离性能的影响,并分析了底膜的孔径、孔隙率、亲疏水性等理化性质对复合膜性能的影响以及不同类型中间层的优缺点。在此基础上,总结了当前业界内亟待解决的问题,并对纳滤膜的未来发展趋势进行了展望。     

新型还原氧化石墨烯/氮化碳复合纳滤膜制备及其性能

高性能石墨烯基复合膜的制备是目前国际研究热点,但是石墨烯基纳滤膜在脱盐中水通量较低,限制其在脱盐中的应用。采用聚多巴胺(PDA)改性聚砜(PSF)膜为基膜,将还原氧化石墨烯(rGO)和超薄氮化碳(uCN)纳米片通过真空抽滤法在基膜表面自组装制备新型还原氧化石墨烯/氮化碳复合纳滤膜。通过场发射扫描电子显微镜、透射电子显微镜、X 射线衍射仪、傅里叶变换红外光谱仪和X射线光电子能谱仪等研究uCN添加对膜结构和形貌的影响,并考察不同uCN添加比例、rGO用量及压力复合纳滤膜性能变化规律。结果显示当在100 mg·L^-1的rGO中添加uCN为20 mg·L^-1时所制备的rGO/uCN复合纳滤膜不仅保持良好盐离子截留率(对Na₂SO₄截留率85.86%,对NaCl截留率30.17%),且水渗透系数是rGO膜的2.15倍(88.50 L·m^-2·h^-1·MPa^-1)。     

荷负电手性壳聚糖纳复合滤膜的制备与性能研究

以聚砜超滤膜作为基膜,以壳聚糖和壳聚糖衍生物的混合物为功能层制备纳滤膜。P2-5复合纳滤（NF）膜对Na2SO4的截留率为93%,相应的通量501.3 L/（m2·h）。电荷效应对NaCl几乎没有影响,而对Na2SO4影响显著。该膜为典型的荷负电膜,适合分离高价阴离子。