聚芳醚酮超滤膜的研究

本文以国产聚芳醚酮为原料，研究了铸膜液组成，聚合物浓度，添加剂种类和用量等对超滤膜性能的影响，选择适宜组成的铸膜液，可以制得截留分子量为２０００，６０００，１００００的超滤膜。上述超滤膜对α－干扰素的分离浓缩效果较好，其截留率均可达到９９％以上。     

大孔径聚砜超滤膜的研究

作者用向铸膜液中加水的方法对制备大孔膜进行了研究。选择适宜的聚砜浓度和水含量，可以制得截留分子量为１５万的聚砜超滤膜。该膜对丙种球蛋白的截留率＞９５％，纯水透水速度可达７０－８０ｍｌ／ｃｍ＾２·ｈ（０．１ＭＰａ）。     

诺氟沙星分子印迹共混膜的制备及应用

本文以诺氟沙星为模板分子,甲基丙烯酸为功能单体,乙二醇二甲基丙烯酸酯为交联剂,采用本体聚合法制备分子印迹聚合物,与聚砜铸膜液混合,制备出可以在低压力下对诺氟沙星有特异性截留作用的分子印迹共混膜.采用红外光谱对共混膜的结构进行表征,利用扫描电子显微镜对共混膜微观形貌进行表征.研究了聚合物的质量分数对共混膜水通量和截留率的...     

聚氯乙烯超过滤膜性能的稳定化

本文着重研究和讨论了聚氯乙烯(PVC)超过滤膜制膜液结构的稳定性,并改进了制膜液的组成.控制PVC在DMA溶剂中的溶解温度和添加剂用量等,是PVC超过滤膜性能稳定化的重要保证.用C_4醇和PEG双组分添加剂,以DMA为溶剂的PVC超过滤膜在0.25mPa压力下,截留率(M=68000)>98％,透水率>25ml/cm~2·h.     

聚砜—磺化聚砜共混超滤膜的研究

本文以聚砜和磺化聚砜为原料，制备了低截留分子量的共混超滤膜，此种膜具有适中透水量，对分子量３０００的ＰＥＧ截留率在９０％以上，对膜的制备参数，如聚合物浓度，不同溶剂，不同添加剂和凝胶介质对膜性能的影响进行了较详细的的研究。     

酚类分子结构和纳滤膜特性对截留率的影响规律

选择21种酚类化合物作为模型污染物,分别测定了三种不同纳滤膜对酚类化合物的截留率.结果表明,酚类化合物截留率受到取代基位置、种类和膜特性的影响.对NF270膜和NF膜而言,截留率从大到小的次序为邻位>间位>对位,而NF90膜的截留率为邻位>对位;供电子取代基有增大截留率的趋势,吸电子取代基有减小截留率的趋势;孔径小、荷电量大的纳滤膜截留率更大.通过基于遗传算法的偏最小二乘回归法(GA-PLS),建立了纳滤膜对酚类化合物截留率的定量构效关系模型,通过分析回归方程,可以看出酚类化合物的pKa值对截留率影响最大,影响较大的还有偶极矩等参数.     

聚砜-磺化聚砜共混超滤膜的研究

本文以聚砜和磺化聚砜为原料,制备了低截留分子量的共混超滤膜,此种膜具有适中透水量,对分子量3000的PEG截留率在90％以上。对膜的制备参数,如聚合物浓度、不同溶剂、不同添加剂和凝胶介质对膜性能的影响进行了较详细的研究。     

不同汲取液在正渗透膜处理垃圾渗滤液过程中的作用

以垃圾渗滤液处理过程中的膜生物反应器(Membrane Bio-Reactor,MBR)出水作为研究对象,采用正渗透膜技术对其进行过滤,对比选择碳酸氢铵和乙二胺四乙酸(Ethylene Diamine Tetraacetic Acid,EDTA)-锌钠两种汲取液中性能较好的进行中试实验。研究了两种汲取液的不同浓度及膜朝向对膜通量的影响,检测了两种汲取液长时间运行所能达到的回收率,分析了两种汲取液的污染物截留率,用斑马鱼胚胎评估了垃圾渗滤液经两种汲取液处理后的生物毒性。结果表明:膜通量随着汲取液浓度增加而增加;在减压渗透(Pressure Reduced Osmosis,PRO)模式下的通量较正渗透(Forward Osmosis,FO)模式高,但污染较严重;碳酸氢铵和EDTA-锌钠在PRO和FO模式下的回收率分别为86.6%、91.6%和66.5%、71.2%;两种汲取液处理后的污染物截留率相差无几,都在98%以上;斑马鱼胚胎暴露于纯水、碳酸氢铵、EDTA钠盐汲取液处理后的水和垃圾渗滤液MBR出水中三天之后存活率为81%、76%、68%和0;实验说明相比于EDTA-锌钠,碳酸氢铵性能较好,适合进行下一步中试试验。     

乳状液膜法萃取氨基酸的研究

本文以ＴＯＭＡＣ为载体，ＥＣＡ４３６０Ｊ为表面活性剂，内外相Ｃｌ＾－浓度梯度为推动力，研究了Ｌ－苯丙氨酸在乳状液膜体系中的传输，并对影响液膜萃取的各种因素进行了系统的阐述，确定了此体系的最佳膜相组成的实验条件，实现了Ｌ－苯丙氨酸的提取和浓缩。     

丙烯腈二元共聚物超滤膜的研制

本文对丙烯腈-甲基丙烯酸甲酯二元共聚物(PAN)超滤膜的成膜过程及膜分离性能进行了研究。结果表明:由PAN-双溶剂-酯类铸膜液制成的超滤膜对牛血清蛋白的截留率(R)为97.62％,通量(f)为84.96ml/cm~2.h.通过电子显微镜扫描观察膜底、表层以及膜断面的结构,对膜的形成机理与膜分离性能进行了研究,证明PAN是一种性能良好的新型膜材料,用PAN二元共聚物超滤膜对α-粉酶进行超滤浓缩试验,取得了较好的结果。     

聚醚砜-磺化聚砜共混膜的研究

利用国内近几年开发的新型膜材料,选择适当的共混聚合物体系,可以制得性能优良的共混膜。本文通过共混方式,制得了孔径较小的共混超滤膜。详细研究了聚醚砜-磺化聚砜共混材料的相溶性、铸膜液组成、蒸发时间和凝胶温度等因素对共混超滤膜分离特性与形态结构的影响。     

丙烯腈—醋酸乙烯二元共聚物超滤膜的制备及其性能表征

本文研究了丙烯腈-醋酸乙烯二元共聚物[P(AN-VAc)]超滤膜及其性能。研究了共聚物材料、铸膜液成份和成膜工艺条件对膜性能的影响,并对膜的物化稳定性和耐菌性能等进行了表征。实验表明,P(AN-VAc)是一种性能良好的膜材料,其对添加剂的适应性尤佳。本文还通过对红外光谱及电子显微镜扫描对膜的结构进行了初步探讨。     

Characterization and performance of nanofiltration membranes

The availability of clean water has become a critical problems facing the society due to pollution by human activities. Most regions in the world have high demands for clean water. Supplies for freshwater are under pressure. Water reuse is a potential solution for clean water scarcity. A pressure-driven membrane process such as nanofiltration has become the main component of advanced water reuse and desalination systems. High rejection and water permeability of solutes are the major characteristics that make nanofiltration membranes economically feasible for water purification. Recent advances include the prediction of membrane performances under different operating conditions. Here, we review the characterization of nanofiltration membranes by methods such as scanning electron microscopy, thermal gravimetric analysis, attenuated total reflection Fourier transform infrared spectroscopy, and atomic force microscopy. Advances show that the solute rejection and permeation performance of nanofiltration membranes are controlled by the composition of the casting solution of the active layer, cross-linking agent concentration, preparation method, and operating conditions. The solute rejection depends strongly on the solute type, which includes charge valency, diffusion coefficient, and hydration energy. We also review the analysis of the surface roughness, the nodule size, and the pore size of nanofiltration membranes. We also present a new concept for membrane characterization by quantitative analysis of phase images to elucidate the macro-molecular packing at the membrane surface.     

PVDF ultrafiltration membranes of controlled performance via blending PVDF-g-PEGMA copolymer synthesized under different reaction times

PVDF blended different graft ratio of PVDF-g-PEGMA were systematically studied. Tuning the amphiphilic copolymer synthesis time to control membrane performance. The PVDF membrane with PVDF-g-PEGMA at 19 h possesses most surface oxygen content. The synthesis time of PVDF-g-PEGMA at 9 h is good for high flux UF membrane. Polyvinylidene fluoride grafted with poly(ethylene glycol) methyl ether methacrylate (PVDF-g-PEGMA) was synthesized using atomic transfer radical polymerization (ATRP) at different reaction times (9 h, 19 h, and 29 h). The corresponding conversion rates were 10%, 20% and 30%, respectively. PVDF was blended with the copolymer mixture containing PVDF-g-PEGMA, solvent and residual PEGMA under different reaction times. In this study, we explored the effect of the copolymer mixture additives with different synthesis times on cast membrane performance. Increasing the reaction time of PVDF-g-PEGMA causes more PVDF-g-PEGMA and less residual PEGMA to be found in the casting solution. Incremental PVDF-g-PEGMA can dramatically increase the viscosity of the casting solution. An overly high viscosity led to a delayed phase inversion, thus hindering PEGMA segments in PVDF-g-PEGMA from migrating to the membrane surface. However, more residual PEGMA contributed to helping more PEGMA segments migrate to the membrane surface. The pure water fluxes of the blended membrane with reaction times of 9 h, 19 h, and 29 h are 5445 L·m⁻²·h⁻¹, 1068 L·m⁻²·h⁻¹and 1179 L·m⁻²·h⁻¹, respectively, at 0.07 MPa. Delayed phase inversion can form smaller surface pore size distributions, thus decreasing the water flux for the membranes with PVDF-g-PEGMA at 19 h and 29 h. Therefore, we can control the membrane pore size distribution by decreasing the reaction time of PVDF-g-PEGMA to obtain a better flux performance. The membrane with PVDF-g-PEGMA at 19 h exhibits the best foulant rejection and cleaning recovery due to its narrow pore size distribution and high surface oxygen content.     

Design of nanofibre interlayer supported forward osmosis composite membranes and its evaluation in fouling study with cleaning

• A fine fibre (40–60 nm diameter) interlayer (~1 µm thickness) was electrospun. • Fine fibre interlayer promoted formation of defect-free dense polyamide layer. • FO membrane with dual-layer substrate had less organic fouling potential. • High reverse salt flux accelerated organic fouling on FO membrane. Nanofibre-supported forward osmosis (FO) membranes have gained popularity owing to their low structural parameters and high water flux. However, the nanofibrous membranes are less stable in long-term use, and their fouling behaviours with foulants in both feed solution (FS) and draw solution (DS) is less studied. This study developed a nanofibrous thin-film composite (TFC) FO membrane by designing a tiered dual-layer nanofibrous substrate to enhance membrane stability during long-term usage and cleaning. Various characterisation methods were used to study the effect of the electrospun nanofibre interlayer and drying time, which is the interval after removing the M-phenylenediamine (MPD) solution and before reacting with trimesoyl chloride (TMC) solution, on the intrinsic separation FO performance. The separation performance of the dual-layer nanofibrous FO membranes was examined using model foulants (sodium alginate and bovine serum albumin) in both the FS and DS. The dual-layer nanofibrous substrate was superior to the single-layer nanofibrous substrate and showed a flux of 30.2 L/m²/h (LMH) when using 1.5 mol/L NaCl against deionised (DI) water in the active layer facing draw solution (AL-DS) mode. In the fouling test, the water flux was effectively improved without sacrificing the water/solute selectivity under the condition that foulants existed in both the FS and DS. In addition, the dual-layer nanofibrous TFC FO membrane was more robust during the fouling test and cleaning.     

铬酸钠共存对铝酸钠溶液种分的影响

研究了铬酸纳共存时对铝酸钠溶液种分的影响，结果表明，含有铬酸钠的铝酸钠溶液中，铝铬比大于３．６时，铬酸钠的存在对铝酸钠种分没有明显影响；铝铬比小于１．８时，铬酸钠的存在对铝酸钠种分有明显影响，本文还试验了选择一定组成的实际铝酸钠溶液，经种分，使铬酸钠与铝酸钠完全有得到了有效分离。     

多功能高铁絮凝剂电化学合成的机理和条件

本文研究了采用电解加复合稳定剂的方法制备ＦｅＯ４＾２－絮凝剂的电化学与溶液化学过程机制，分析了ＯＨ＾－膜平衡过程对ＦｅＯ４＾２－形成的影响，探讨了ＦｅＯ４＾２－水溶液分解的诱发因素，初步确定了ＦｅＯ４＾２－电化学合成的最佳条件。研究结果表明，适宜的电量参数，合理的电解液组成和高效的ＯＨ＾－膜渗透是顺利进行稳定化ＦｅＯ４＾２－电解合成的三个要素。     

液膜法处理硫普罗宁废水的研究

采用W／O型乳状液膜法提取水溶液中的硫普罗宁,考察了载体、温度、硫普罗宁浓度以及油内比、试剂比、乳水比对提取率的影响,并得出了液膜法提取硫普罗宁的最佳乳液配方：油内比＝1：1,乳水比＝1：2,试剂比＝6－8,载体浓度＝5％,温度20℃,转速＝240－250r.min^-1,其提取率高达90％。     

乳化液膜法提取苯酚的动力学研究

研究了以双丁二烯亚胺－煤油作膜相,ＮａＯＨ溶液为内水相的乳化液膜提取苯的动力学特性,测定了膜相与内外水相组成,搅拌速度,温度对提取速率的影响,得出了提取速率规律。