多通道陶瓷超滤膜孔径分布及截留率测定

本文对工业化多通道陶瓷超滤膜进行了研究,以异丁醇－蒸馏水体系用液－液排除法测定了超滤膜的孔径及孔径分布,对同一膜管及体系,进行了重复性实验,测定了膜的截留率,比较了截留率与孔径及孔径分布的关系,讨论了操作条件对截留率的影响,为工业化膜的制备及选取提供指导。     

液液界面法测超滤膜孔径及孔径分布

本采用液液界面法，利用毛细管现象测定了截留分子量为２×１０＾４和５×１０＾４聚砜超滤膜ＰＳ－２，ＰＳ－５的孔径及孔径分布。结果表明，利用水－正丁醇体系能测定超滤膜的孔径及孔径分布，并且具有操作简便，测试压力接近膜工作压力的优点，对于ＰＳ－２超滤膜，测试压力达０．５ＭＰａ即能得到膜完整的孔径分布曲线。     

用光干涉法测定极稀聚乙二醇水溶液的浓度

在超滤膜分离技术中,测定膜孔径是一个重要环节。最常采用测定膜对不同分子量聚乙二醇的截留量来判断膜孔径的大小,而截留量又与溶液浓度有关。因此,精确测定水中微量聚乙二醇的浓度是确定膜孔径大小的关键步骤。采用阿贝折射仪测定聚乙二醇浓度误差大,而比色法测定操作繁复、精度也不高。我们采用光干涉法测定水中微量聚乙二醇的含量。该法操作简便、快速、测量准确,为膜孔径的测定提供了一个较理想的方法。     

聚砜酰胺的分子量对其超滤膜性能的影响——Ⅱ.膜性能与成膜机理

研究了PSA的分子量对其超滤膜性能的影响,发现PSA分子量高,膜孔径大、分布宽;分子量低,膜孔径小、分布窄;但分子量过低,孔径变大,且分布宽。并就分子量对PSA超滤膜的透水率、截留率、压实性能,以及制膜液的相分离等性能进行比较,讨论成膜机理,改进了的成膜机理较好地解释了实验结果。     

γ—Al2O3陶瓷膜制备与性能的初步研究

以无机聚合铝浸渍液，以多孔素烧陶瓷板的为基片，采用原位造粒法制备γ－Ａｌ２Ｏ３陶瓷膜，测试了所制膜的气体和水的渗透率，最大孔径，平均孔径及聚乙二醇的截留率－分子量关系，并用扫描电镜观察了膜的微观结构。     

醋酸纤维素—纤维素增强膜的结构特征和分离性能

本文描述了醋酸纤维素－纤维素大孔增强超滤膜的结构特征一分离性能之间的关系。详细论述了膜材料含量和粘连剂含量及其分子量对膜结构和性能的影响。论述了不同配方铸膜液的膜，其孔径，水通量和截留率随操作压力的变化规律。实验证明这种高强度的ＣＡＣ膜经多次重复使用后，其结构性能保持完好。     

复合中空纤维超滤膜的研制

本文就复合中空纤维超滤膜的制备工艺和成膜条件对膜性能影响进行了系统的研究，实验表明，对外压式中空纤维膜，内凝固液条件的改变，主要影响复合膜的内致密层，进而影响膜的透过通量，但对膜的截留孔径无影响，随空中行走距离增大，膜的透过通量减小，截留孔径增大。另外，通过基膜的选定与内凝固液的调节，复合中空纤维膜的分离孔径主要取决于复合层膜，即在适宜的条件下，基膜不影响复合膜的分离孔径，同时也不决定复合中空纤维     

中空纤维膜孔径及其分布的测定

研究了中空纤维膜孔径及其分布的测定方法．液液置换法。通过研究建立了能够准确描述跨膜压差与流体通量的数学模型,采用不同的液液体系（正丁醇．纯净水、正戊醇．纯净水和正己醇一纯净水）测定了膜孔径为0.2μm的中空内压疏水膜的孔径及其分布,并对测试结果进行比较分析。实验研究结果与电镜扫描结果符合较好,研究表明液液置换法装置简单、易操作、是一种理想的膜孔径分布表征方法。     

不同标准物表征超滤膜截留性能的比较

本文用蛋白，聚乙二醇和葡聚糖三种不同溶质对聚砚，聚砚酰胺及磺化聚砚三种超滤膜的截留率－分子量曲线进行了测定。对同一种膜，具有相同分子量的不同溶质来说，它们的截留率是不同的。膜对蛋白的截留率高于它对聚乙二醇和葡聚糖的截留率。     

用于碱纤压榨液过滤的纳滤膜技术

1 纳滤膜概述及原理 纳滤是在压差推动力作用下，盐及小分子物质透过纳滤膜，而截留大分子物质的一种液液分离方法，又称选择性反渗透。纳滤膜截留分子量范围为200～1000／MWCO，介于超滤和反渗透之间，主要应用于溶液中大分子物质的浓缩、分离和纯化。     

Cellulose acetate and sulfonated polysulfone blend ultrafiltration membranes. II. Pore statistics,molecular weight cutoff,and morphological studies

The determination of the pore size, porosity, number of pores, molecular weight cutoff (MWCO), and morphology of an ultrafiltration membrane is necessary for predicting the performance of a membrane for a specific application. For ultrafiltration membranes prepared from cellulose acetate and sulfonated polysulfone in the presence and absence of various concentrations of the additive poly(ethylene glycol) 600, pore statistics and MWCOs were determined in studies with dextrans of different molecular weights. Surface and cross‐sectional morphologies of the membranes were analyzed with scanning electron microscopy at different magnifications. The pore size increased with increasing concentrations of sulfonated polysulfone and additive in the casting solution. Similarly, the MWCOs of the membranes ranged from 19 to 150 kDa, depending on the various polymer blend compositions and additive concentrations. Results from scanning electron microscopy provided qualitative evidence for the trends observed for the pore statistics and MWCO results. © 2002 Wiley Periodicals, Inc. J Appl Polym Sci 84: 430–444, 2002; DOI 10.1002/app.10414     

Modeling of the Relationship Between Pore Size Distribution and Thickness of Ceramic MF Membrane

The pore size distribution(PSD)measured by the gas bubble point(GBP)method ofceramic microfiltration(MF)membranes prepared by suspension technique was found to be signifi-cantly influenced by the membrane thickness.A culm-like model for pore structure was introduced tocharacterize the membrane pores instead of the conventional model which does not reflect the radiusvariation along the pore passages and is unable to explain the thickness effect on the membrane PSD.A laminate structure,taking the culm-like model for pore structure into consideration,was hypoth-esized for ceramic MF membranes.A mathematical model was then established to quantitativelydescribe the relationship between the membrane number PSD and the membrane thickness.Goodresults were obtained for the correlation of mean pore size and simulation of the PSD for ceramicMF membranes.     

致密超细球形氧化铝制备性能良好的陶瓷超滤膜

热等离子体制备的超细球形氧化铝具有表面致密光滑、分散性好等特点,本工作以超细球形氧化铝为原料,通过浸渍提拉烧结法,制备了孔径分布窄、渗透通量高的陶瓷超滤膜,研究了烧结温度对陶瓷膜微孔结构的演化、孔径分布和渗透通量的影响。随后对1250℃下烧结的陶瓷膜进行了纳米硅水分散液过滤处理,采用不同堵塞模型分析了陶瓷膜过滤纳米硅水分散液的膜污染过程。结果表明,通过调节烧结温度调控陶瓷膜的微孔结构,当烧结温度为1250℃时,陶瓷膜的孔径分布较窄,孔径大小为25?65 nm,渗透通量为986.4 L/(m2?h)。超细球形氧化铝粒径分布较窄及表面致密光滑有助于1250℃下烧结形成均匀的烧结颈,提供了陶瓷膜较窄的孔径分布。对1250℃下烧结的陶瓷膜进行了纳米硅水分散液过滤处理后其浊度下降为0.231 NTU,浊度去除率达99.96%。采用不同堵塞模型分析了陶瓷膜过滤纳米硅水分散液的膜污染过程,结果表明,纳米硅水分散液的堵塞模型是滤饼过滤,属于可逆污染。     

Design and fabrication of whisker hybrid ceramic membranes with narrow pore size distribution and high permeability via co-sintering process

Ceramic microfiltration membranes (MF) with narrow pore size distribution and high permeability are widely used for the preparation of ceramic ultrafiltration membranes (UF) and in wastewater treatment. In this work, a whisker hybrid ceramic membrane (WHCM) consisting of a whisker layer and an alumina layer was designed to achieve high permeability and narrow pore size distribution based on the relative resistance obtained using the Hagen-Poiseuille and Darcy equations. The whisker layer was designed to prevent the penetration of alumina particles into the support and ensure a high porosity of the membrane, while the alumina layer provided a smooth surface and narrow pore size distribution. Mass transfer resistance is critical to reduce the effect of the membrane layers. It was found that the resistance of the WHCM depended largely on the alumina layer. The effect of the support and whisker layer on the resistance of the WHCM was negligible. This was consistent with theoretical calculations. The WHCM was co-sintered at 1000?°C, which resulted in a high permeability of ~?645?L?m^?1 h^?1 ;bar^?1 and a narrow pore size distribution of ~?100?nm. Co-sintering was carried out on a macroporous ceramic support (just needed one sintering process), which greatly reduced the preparation cost and time. The WHCM (as the sub-layer) also showed a great potential to be used for the fabrication of ceramic UF membranes with high repeatability. Hence, this study provides an efficient approach for the fabrication of advanced ceramic MF membranes on macroporous supports, allowing for rapid prototyping with scale-up capability.     

颗粒粒径和膜孔径对陶瓷膜微滤微米级颗粒悬浮液的影响

通过测定颗粒悬浮液通过陶瓷微滤膜时的参透通量及污染阻力,确定了陶瓷膜处理微米级颗粒悬浮液时,颗粒粒径和膜孔径对微滤过程的影响和膜污染机理,获得了微米级颗粒悬浮液微滤过程中膜孔径的选择方法。     

The effects of air gap length on the internal and external morphology of hollow fiber membranes

A systematic study of the air gap effects on both the internal and the external morphology, permeability and separation performance of polyvinylidene fluoride (PVDF) hollow fiber membranes has been carried out. The hollow fibers were prepared using the dry-jet wet spinning process using a dope solution containing PVDF/ethylene glycol/N, N-dimethylacetamide with a weight ratio of 23/4/73. Ethanol aqueous solution, 50% by volume, was used as internal and external coagulants. The inner and the outer surfaces of the prepared hollow fibers were analyzed by atomic force microscopy (AFM), while their cross-sectional structure was studied by scanning electron microscopy (SEM). Ultrafiltration experiments were conducted using non-ionic solutes of different molecular weights. The results show that both the pore sizes and nodule sizes have a log-normal distribution. The pore size, nodule size and roughness parameters of the inner and outer surfaces of the hollow fibers were affected by the air gap distance. Alignment of nodules to the spinning direction was observed. Experimental results indicate that an increase in air gap distance, from 1 to , results in a hollow fiber with a lower permeation flux and a higher solute separation performance due to the decrease of the pore size. AFM analysis reveals that the air gap introduces an elongational stress because of gravity on the internal or external surfaces of the PVDF hollow fibers. At low air gap distance, the inner surface controls the ultrafiltration performance of the PVDF hollow fiber membranes because of its lower pore size, while at high air gap lengths the inner pore size becomes larger than the outer pore size. The turning point was observed at an air gap distance of .     

Ultrafiltration: a means for decolorization of cane sugar solution

Membrane ultrafiltration was used for clarification as well as for decolorization of raw brown sugar obtained from the Indian sugar industry. Experimental results were obtained using sugar solutions of 28 and 46°Brix and mineral membranes of 20 nm, 5 and 1 kDa molecular weight cut-off (MWCO) on an industrial size pilot plant under different operating conditions. It was found that, even with the membrane of MWCO of 1 kDa, the maximum color removal was limited to 58.67% and steady-state permeate flux was only 29 1/h m² for the 46°Brix sugar solution. Empirical relationships between membrane performance (for decolorization and clarification) and membrane pore diameter were obtained from the experimental results. In order to obtain very high quality white crystalline sugar, further processing with adsorbents or use of an ion-exchange technique is required.     

Thin-film nanofibrous composite membranes containing cellulose or chitin barrier layers fabricated by ionic liquids

The barrier layer of high-flux ultrafiltration (UF) thin-film nanofibrous composite (TFNC) membranes for purification of wastewater (e.g., bilge water) have been prepared by using cellulose, chitin, and a cellulose-chitin blend, regenerated from an ionic liquid. The structures and properties of regenerated cellulose, chitin, and a cellulose-chitin blend were analyzed with thermogravimetric analysis (TGA) and wide-angle X-ray diffraction (WAXD). The surface morphology, pore size and pore size distribution of TFNC membranes were determined by SEM images and molecular weight cut-off (MWCO) methods. An oil/water emulsion, a model of bilge water, was used as the feed solution, and the permeation flux and rejection ratio of the membranes were investigated. TFNC membranes based on the cellulose-chitin blend exhibited 10 times higher permeation flux when compared with a commercial UF membrane (PAN10, Sepro) with a similar rejection ratio after filtration over a time period of up to 100 h, implying the practical feasibility of such membranes for UF applications.