亲水膜的表面改性及在膜蒸馏中的应用

膜的微孔性和疏水性是水溶液膜蒸馏的两个基本条件,迄今人们均采用疏水性高分子材料制成疏水微孔膜用于膜蒸馏研究。本文采用辐照接枝聚合和等离子体表面聚合的方法,将亲水的醋酸纤维素微孔膜和硝酸纤维素微孔膜表面疏水化改性,成功地用于膜蒸馏研究,大大扩展了疏水微孔膜的材料来源。实验结果表明,亲水膜表面改性得到的疏水膜,其膜蒸馏性能不低于疏水材料制成的膜,尤其是等离子体聚合法可以实现多种特殊单体在多孔的材料表面聚合,成为制备高性能疏水微孔膜的有效手段,为膜蒸馏的深入发展和实用化创造了有利条件。     

氯化锂为添加剂制得的疏水聚偏氟乙烯不对称微孔膜的形态结构及其膜蒸馏性能

结合膜的形态结构研究了以 LiCl为添加剂制得的疏水 PVDF膜的膜蒸馏性能。与来用水溶液高分子添加剂制得的PVDF微孔膜相比,膜蒸馏性能有了较大提高,尤其具有更高的截留率。制得的微孔膜的蒸馏通量已接近商品膜的膜蒸馏通量,表明以LiCl为添加剂制得的PVDF疏水微孔膜是一种适用于膜蒸馏的较理想的疏水微孔膜。     

聚偏氟乙烯膜蒸馏技术在水处理中的应用研究进展

膜蒸馏是一种以膜为介质,利用传统蒸发工艺开发的新型膜分离技术。随着高分子材料行业的进步和制膜工艺的成熟,膜蒸馏技术取得了巨大的进展,在水处理领域拥有十分广阔的市场前景。膜蒸馏技术的核心是膜的通量和使用寿命,而性能优良的膜材料是膜蒸馏技术发展的关键。聚偏氟乙烯(PVDF)因具有成膜性能好、表面张力大、化学稳定性强等优点,在膜蒸馏技术应用研究中备受青睐。同时PVDF与其他聚合物具有良好的相容性,为膜的改性研究奠定了基础,极大地扩展了应用范围。本文介绍了膜蒸馏技术的工作原理及工艺特点以及PVDF膜材料的特点及改性方法,重点对PVDF膜蒸馏技术在水处理领域的应用进行了梳理和总结,讨论了该技术亟待研究和解决的问题,以期为该工艺技术的进一步发展提供科学支撑和理论依据。     

聚酰亚胺微孔膜疏水化用于膜蒸馏

采用聚合物表面涂覆改性的方法，将疏水性聚合物硅橡胶涂覆在聚酰亚胺亲水微孔膜上，制得了具有良好膜蒸馏性能的聚酰亚胺疏水微孔复合膜。研究了涂覆工艺条件对所得聚酰亚胺疏水微孔复合膜的膜蒸馏性能的影响。结果表明，控制适当工艺条件可制得具有高膜蒸馏通量的聚酰亚胺微孔复合膜，其透过系数可达２．１７×１０－３ｋｇ／ｍ２·ｈ·Ｐａ。该改性聚酰亚胺疏水微孔复合膜使用３７ｄ后，截留率仍保持在９９．５％以上，具有较长使用寿命。     

应用于膜蒸馏过程的F26微孔膜的初步研究

以N-甲基吡咯酮作为溶剂 ,丙酮为溶胀剂 ,聚乙二醇 4 0 0为添加剂利用相转换法制备出偏氟乙烯 六氟丙烯共聚物 (F2 6 )的疏水微孔膜并且应用在膜蒸馏过程中 .研究了丙酮以及N 甲基吡咯酮 丙酮体系对膜参数以及结构的影响 .通过SEM观察了膜的微观结构 ,发现用N 甲基吡咯酮 丙酮体系制得的微孔膜兼具指状孔和海绵状孔结构 .无添加剂条件下制得的F2 6膜其对蒸馏水的接触角比相同条件下制备的PVDF膜大 .在用相转换法制备的F2 6和PVDF的疏水膜中 ,选择具有适当孔径结构的微孔膜用于膜蒸馏实验 ,F2 6膜的膜蒸馏系数比PVDF膜来得大 ,相同操作条件下的膜蒸馏通量也比PVDF膜高 .     

聚合物层状组装膜

介绍了近几年来我们研究组在层状组装膜的构筑以及功能化研究方面取得的一些最新进展.包括结合表面溶胶-凝胶技术与静电层状组装技术,实现了二阶非线性基团在层状组装多层膜中的非对称排列,制备了具有二阶非线性效应的膜材料;采用室温压印技术,发展了一种简便、经济和具有普适性的层状组装聚合物膜图案化方法;以轻度交联的聚合物微凝胶为构筑基元,制备了具有高负载量的聚合物层状组装膜;发展了一种基于离子剥离技术的层状组装自支持膜制备方法;基于层状组装技术,制备了具有超疏水和抗反射功能的涂层.     

分离液体的膜

本文概述了7种以高分子为膜材料、用于混合液体分离的膜分离过程,即离子交换膜与电渗析、反渗透、超滤、微孔过滤、膜萃取、渗透汽化和膜蒸馏。对其原理、高分子膜材料、应用和发展趋向作了简要介绍;并阐述了我国膜分离发展的现状和展望。     

等离子体聚合法制备膜蒸馏用疏水微孔复合膜

本文以八氟环丁烷为单体,采用等离子体聚合法将亲水性硝酸纤维素微孔膜改性,制得疏水硝酸纤维素微孔复合膜。所得疏水微孔复合膜可用于膜蒸馏,并具有优良的膜蒸馏性能,其通量达到反渗透水平。利用扫描电镜、X-射线显微分析和XPS等分析手段研究了聚合条件对所得复合膜结构性能的影响.     

溶剂散逸自组装制备超疏水针垫阵列膜

利用溶剂散逸自组装方法,以聚苯乙烯、聚十二烷基丙烯酰胺-6-丙烯酰胺基己酸（CAP）和三氯甲烷为原料,在平滑的固体基质上制备了有序多孔膜,该膜上下表面可在外力作用下发生分离,得到具有微米级超疏水针垫阵列膜。 结果表明,制得的聚苯乙烯膜具备超疏水性质,与水接触角达158°。     

超润湿膜在乳化液破乳中的应用及作用机制

超润湿膜材料由于对水和油有独特的润湿性质,可显著提高膜材料处理乳化液的通量,有效缓解严重的膜污染问题,因此在乳化液废水处理领域受到越来越多的重视。本文从超润湿膜的设计制备、分离效果和作用机制三个方面进行分析和总结。超润湿膜材料包括超亲水膜、Janus膜和功能位点膜,主要通过构建亲水表面和粗糙结构进行膜的设计制备,其中静电纺丝法合成的交联纤维膜由于可以突破筛分效应对膜孔径的限制,在乳化液分离中具有较好的应用前景。同时,归纳超亲水膜的滤水破乳模式和Janus膜的集油破乳模式,前者具有操作压力低、过滤通量高、抗污染性能好的特点,后者具有高纯度集油的特点;并分析膜润湿性、膜孔径、膜上功能位点等膜结构性质和表面活性剂浓度大小等因素对乳化液破乳分离效能的影响规律。最后,总结液滴在膜垂向和切向上的迁移转化规律,以及在Janus膜集油破乳过程中液滴穿透过膜的机制及其力学分析探讨,该部分研究当前主要是基于液滴形态变化的推测和力学的定性分析,对于相关机制的实证和定量的力学分析还有待进一步探究。     

荷电膜的膜电位研究进展

膜电位的测定是表征荷电膜的传递现象的重要参数之一。本文简要介绍了膜电位理论基础,包括T. M. S.理论和不可逆热力学理论。分别阐述了关于离子交换膜、双极膜、两性膜以及复合膜的膜电位的最新进展,并提出今后的发展方向。     

透氢钯复合膜的原理、制备及表征

钯及其合金膜由于具有透氢性好和耐高温的特点,除了用作氢气分离和纯化器外,还可以用作脱氢、制氢等反应的反应器,以实现反应和分离的一体化,并提高转化率和选择性。本文综述了钯基复合膜的原理、制备及表征,并重点介绍了本研究组的光催化镀膜工艺。     

高分子纳滤膜的研究及进展

对高分子纳滤膜的发展背景以及国内外在这一领域的研究的研究进展作了详细的介绍。     

透氢钯复合膜的原理、制备及表征

钯及其合金膜由于具有透氢性好和耐高温的特点,除了用作氢气分离和纯化器外,还可以用作脱氢、制氢等反应的反应器,以实现反应和分离的一体化,并提高转化率和选择性。本文综述了钯基复合膜的原理、制备及表征,并重点介绍了本研究组的光催化镀膜工艺。     

纳米复合膜在膜分离领域的研究进展

基于纳米材料的独特性质,将其引入高分子膜所制得的纳米复合滤膜有望解决目前制约膜技术发展的“上限平衡”问题。 本文综述了碳纳米管、石墨烯、SiO2、TiO2、分子筛、ZrO2以及纳米银颗粒等纳米复合膜在膜分离领域的研究进展。 这些纳米材料对于提高复合膜的机械稳定性、亲水性、选择性、渗透性及抗污染能力等有显著的效果。 此外,对纳米复合膜的发展与应用做了展望,也对其研究中存在的问题和解决方法进行了阐述。     

Preparation of Zeolite X Membranes on Porous Ceramic Substrates with Zeolite Seeds

Zeolite X membranes were investigated by in-situ hydrothermal synthesis on porous ceramic tubes precoated with zeolite X seeds or precursor amorphous aluminosilicate, and porous α-Al2O3 ceramic tubes with a pore size of 50 200 nm were employed as supports. Zeolite X crystals were synthesized by the classic method and mixed into deionized water as a slurry with a concentration of 0.2 0.5wt%, having a range of crystal sizes from 0.2 to 2μm. Crystal seeds were pressed into the pores near the inner surface of the ceramic tubes, and crystallization took place at 95℃ for 24-96 h. It was also investigated that Boehmite sol added with zeolite X seeds was precoated on ceramic supports to form a layer of γ-Al2O3 by heating, and hydrothermal crystallization could then take place to prepare the zeolite membranes on the composite ceramic tubes. The crystal species were characterized by XRD, and the morphology of the supports subjected to crystallization was characterized by SEM. The composite zeolite membranes have zeolitic top-layers with a thickness of 10-25 μm, and zeolite crystals can be intruded into pores of the supports as deeply as 100μm. The experimental results indicate that the precoating of zeolitic seeds on supports is beneficial to crystallization by shortening the synthesis time and improving the membrane strength. The resulting zeolite X membrane shows permselectivity to tri-n-butylamine((C4H9)3N) over perfluro-tributyl-amine ((C4Fg)3N), and a permeance ratio of 57 for ((C4Hg)3N to (C4F9)3N could be reached at 350℃. Permeances of BZ, EB and TIPB through the zeolite membrane were also measured and were found to slightly increase with temperature.     

PREPARATION OF SILICALITE-1 AND ZSM-5 ZEOLITE/ CERAMIC COMPOSITE MEMBRANES

ＰＲＥＰＡＲＡＴＩＯＮＯＦＳＩＬＩＣＡＬＩＴＥ┐１ＡＮＤＺＳＭ┐５ＺＥＯＬＩＴＥ／ＣＥＲＡＭＩＣＣＯＭＰＯＳＩＴＥＭＥＭＢＲＡＮＥＳＺｈａｎｇＬｉｘｉｏｎｇ，ＪｉａＭｅｎｇｄｏｎｇ，ＭｉｎＥｎｚｅ（ＲｅｓｅａｒｃｈＩｎｓｔｉｔｕｔｅｏｆＰｅｔｒｏｌｅ...     

Preparation of Zeolite X Membranes on Porous Ceramic Substrates with Zeolite Seeds

Zeolite X membranes were investigated by in-situ hydrothermal synthesis on porous ceramic tubes precoated with zeolite X seeds or precursor amorphous aluminosilicate, and porous α-Al2O3 ceramic tubes with a pore size of 50-200 nm were employed as supports. Zeolite X crystals were synthesized by the classic method and mixed into deionized water as a slurry with a concentration of 0.2-0.5wt%, having a range of crystal sizes from 0.2 to 2μm. Crystal seeds were pressed into the pores near the inner surface of the ceramic tubes, and crystallization took place at 95℃ for 24-96 h. It was also investigated that Boehmite sol added with zeolite X seeds was precoated on ceramic supports to form a layer of r-Al2O3 by heating, and hydrothermal crystallization could then take place to prepare the zeolite membranes on the composite ceramic tubes. The crystal species were characterized by XRD, and the morphology of the supports subjected to crystallization was characterized by SEM. The composite zeolite membranes hav     

Theoretical analysis of the performance of composite membrane consisting of the catalytic and nanofiltration layers

A model of the composite membrane consisting of the catalytic layer (CL) and the nanofiltration layer (NFL) is presented. It has been found that applying NFL on the permeate side of CL it is possible to enhance substantially the conversion of substrate into the product. The best performance is obtained for high retention of substrate and low of product. At higher values of volume flow and/or longer catalytic path the retention degree of product becomes negligible. The presence of NFL enhances the influence of distribution of the reaction rate constant, k, on the conversion ratio. Comparing to k = constant the positive effect is obtained if k increases along the catalytic pore, whereas negative—if k decreases.