溶剂对相分离法制备聚偏氟乙烯微孔膜性质的影响

研究了用相转换法制备聚偏氟乙烯（PVDF）微孔膜时溶剂对成膜性质的影响.用浊点法测定了二甲基亚砜、N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、N-甲基吡咯烷酮、磷酸三甲酯等五种溶剂配制的质量分数为wPVDF=0.12的铸膜液在30℃时的相分离点,显微镜拍照法测定了这些铸膜液与水接触时相分离前沿推进速率,泡点法测定了膜孔径,并测定了气体通量.结果表明,二甲基亚砜、磷酸三甲酯、N,N-二甲基乙酰胺是适于制作聚偏氟乙烯微孔膜的溶剂.     

热致相分离法制聚偏氟乙烯微孔膜稀释剂的选择

依据聚偏氟乙烯(PVDF)、邻苯二甲酸二甲酯、水杨酸甲酯、卡必醇醋酸酯、三醋酸甘油酯、邻苯二甲酸二正丁酯(DBP)、苯乙酮和二苯甲酮(DPK)的Hansen溶度参数及其相对介电常数, 选择能与PVDF以液-液相分离机理进行热致分相的稀释剂, 制备了具有双连续结构的微孔膜. 通过比较PVDF-稀释剂间的溶度参数及相对介电常数的差异, 发现PVDF-DBP体系和PVDF-DPK体系有发生热致液-液相分离的可能. 实时观察上述两个体系的分相过程并测定其结晶温度, 当PVDF质量分数低于30%时, 随着温度的降低, PVDF-DPK体系发生液-液相分离. 根据PVDF-DPK体系相图, 通过控制PVDF含量和降温条件, 无须添加非溶剂或拉伸工艺, 就可以制备出具有双连续结构的PVDF微孔膜.     

聚偏氟乙烯-稀释剂间介电常数差异对热致相分离法制膜微观结构的影响

采用1,4-丁内酯、邻苯二甲酸二甲酯、水杨酸甲酯、邻苯二甲酸二丁酯、三醋酸甘油酯和卡必醇醋酸酯作为稀释剂, 研究了在以热致相分离(TIPS)法制备聚偏氟乙烯(PVDF)微孔膜过程中, 聚偏氟乙烯-稀释剂间介电差异对PVDF膜微观结构的影响. 实验发现, PVDF-稀释剂间介电常数的差异与PVDF膜微观结构有一定关联. 当PVDF介电常数大于稀释剂的介电常数时, PVDF的分子间作用以引力为主导, PVDF分子易于聚集结晶, 形成松散球粒结构. 当PVDF介电常数与稀释剂的介电常数相近时, PVDF的分子间引力作用与斥力作用相均衡, 在淬冷条件下可形成近似双连续结构. 当PVDF介电常数小于稀释剂的介电常数时, PVDF分子间有一定的斥力效应, PVDF分子结晶困难.     

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。     

聚偏氟乙烯电纺膜及其电化学性能的研究

用电纺的方法制备了聚偏氟乙烯纳米纤维膜,它们具有多微孔结构,能够作为锂电池聚合物电解质.电纺中聚合物溶液的浓度对制备的电纺膜的结构形态有很大的影响,低浓度(10 wt%)时得到珠丝结构的膜,浓度15 wt%时则为纤维结构,而高浓度(18 wt%)时,电纺膜为交联的网状结构.用电纺法制备的聚偏氟乙烯纳米纤维微孔膜具有较高的孔隙率,而且它们与锂金属电极具有良好的界面稳定性;在25℃时吸液率最高可达340%,以这种膜制备的聚合物电解质室温电导率可达到1.57×10-3S.cm-1;由该电解质组装的扣式电池以0.5 mA.cm-2恒流充放电,25℃时50次循环后几乎无容量损失,具有良好的循环性能;即使60℃时,电池仍能保持良好的工作稳定性.     

聚偏氟乙烯膜的改性研究进展

主要介绍了聚偏氟乙烯(PVDF)膜在近年来改性方法的最新研究进展,从辐照改性、等离子体改性、共混改性和化学改性等几方面进行了详细介绍,简要介绍了PVDF膜作为离子交换膜的一些最新应用.     

热致相分离法高效制备压电聚偏氟乙烯膜

以环保溶剂乙酰柠檬酸三丁酯(ATBC)为稀释剂,绿色无毒的离子液体1-丁基-3-甲基咪唑六氟磷酸盐([BMIM][PF₆])为添加剂,采用热致相分离(TIPS)法制备聚偏氟乙烯(PVDF)微滤膜,通过扫描电子显微镜观察不同添加剂含量PVDF膜的微观形貌;通过超滤杯对PVDF膜的纯水通量进行了测试;使用拉力计对PVDF膜的机械性能进行了表征;通过红外光谱和X-射线衍射研究了添加剂对PVDF膜晶型结构的影响。结果表明：加入1.0%[BMIM][PF₆]时,PVDF的晶型变为β- 晶型。     

聚偏氟乙烯MBR膜制备及改性研究进展

膜生物反应器技术作为一种新型、高效的水处理技术,已成功应用于废水处理系统。在膜分离工程领域,聚偏氟乙烯(PVDF)作为一种优异的膜材料,成为人们热衷的研究对象。本文综述了目前应用于MBR的PVDF膜制备方法,重点介绍了Fe(OH)3、TiO2t、ween-20+戊二醛、PEBAX、PVDF-g-POEM、PVDF-g-PEGMA、TPU、Al2O3、SiO2微粒等对PVDF膜的改性研究,并对PVDF制备MBR膜的发展前景进行了展望。经过改性后的膜在一定程度上能够有效增强亲水性和抗污染能力,延长膜的寿命,降低运行成本,而且出水水质更好,若增强其机械强度,将会有更广泛的用途。     

聚偏氟乙烯微孔膜的亲水化改性及功能化研究进展

聚偏氟乙烯(PVDF)微孔膜的亲水化改性方法有物理共混、化学共聚、表面涂覆、表面化学处理、表面接枝等几种。其中物理共混和表面涂覆法比较成熟且已获得应用，而PVDF微孔膜的表面化学处理、等离子体或光引发改性技术以及环境敏感性等将成为PVDF微孔膜的改性和功能化研究的主要方向。     

热致相分离聚丙烯微孔膜

对聚丙烯－稀释剂体系热致相分离过程制备聚丙烯微孔膜的意义、原理、过程及研究现状进行了评述。     

热致相分离法制备聚烯烃微孔膜研究进展

非极性及弱极性的结晶高聚物常温下无合适的良溶剂,所以无法使用传统的非溶剂致相分离法制取微孔膜,而近年来发展的热致相分离法解决了这一问题。研究发现聚乙烯、聚丙烯、乙烯．乙烯醇共聚物、乙烯．丙烯酸共聚物、聚(4-甲基-1-戊烯)等聚烯烃是可采用热致相分离法制备微孔膜的材料。本文综述了近年来在热致相分离法制备聚烯烃微孔膜方面的研究进展,重点介绍各种制膜材料(聚合物、稀释剂、萃取剂和助剂)与各种制膜工艺对制得的聚烯烃微孔膜孔径、膜通量和非对称结构等的影响。     

热致相分离法制备聚合物微孔材料

热致相分离是一种制备聚合物微孔材料的有效方法。本文介绍了聚合物初始浓度、聚合物分子量、稀释剂、冷却速率、萃取剂、聚合物密度等因素对热致相分离法制备聚合物微孔材料的影响,并对热致相分离法制备新型微孔材料的最新研究进展进行了综述。     

聚合物分子量对热致相分离法制备聚乙烯微孔滤膜的影响

选取不同分子量的聚乙烯/二苯醚作为聚合物稀释剂体系,通过浊点及结晶温度绘制了体系的热力学相图;并在不同淬冷温度下,通过热致相分离法制备了聚乙烯微孔滤膜。讨论了聚合物分子量及淬冷温度对成膜孔结构的影响。结果表明:聚合物的分子量不仅影响微孔滤膜断面的孔径,还影响其形态和结构。     

热致相分离法制备乙烯-三氟氯乙烯共聚物微孔膜

通过热致相分离法制备了乙烯-三氟氯乙烯共聚物(ECTFE)微孔膜, 考察了ECTFE与不同溶剂的相互作用参数对ECTFE/溶剂体系的液液相区的影响, 通过相容性分析及对ECTFE微孔膜断面结构的观察, 筛选出能与ECTFE发生明显液液相分离的溶剂--邻苯二甲酸二乙酯(DEP). 热力学相图证明, ECTFE/DEP体系具有较宽的液液相分离区, 偏晶点所对应的ECTFE质量分数高达55%. 考察了冷却条件对\{ECTFE/DEP体系膜断面结构的影响, 结果表明, 膜断面孔径随着淬冷温度的降低而减小, 在淬冷温度为458 K时膜断面孔径随粗化时间的增加而增大.     

Polysulfone Membranes via Thermally Induced Phase Separation

Polysulfone (PSF) membranes have gained great attention in the fields of ultrafiltration,microfiltration,and thin film composite membranes for nanofiltration or reverse osmosis.For the first time,it is proposed to fabricate PSF membranes via thermally induced phase separation (TIPS) process using diphenyl sulfone (DPSO2) and polyethylene glycol (PEG) as mixed diluent.DPSO2 is chosen as a crystallizable diluent,while PEG is considered in terms of molecular weight (Mw) and dosage.We systematically investigate the interactions between PSF,DPSO2 and PEG based on the simulation calculations and solubility parameter theory.It is inferred that DPSO2 has an excellent compatibility with PSF,and the addition of PEG results in the ternary system thermodynamically less stable and then facilitates its liquid-liquid (L-L) phase separation.SEM images indicate that cellular-like pores are obvious throughout the membrane when the PEG content in the mixed diluent is 25 wt％-35 wt％.We can facilely manipulate the pore size,water flux and mechanical properties of PSF membranes with the dosage of PEG-200,the Mw of PEG or the cooling rate.The successful application of TIPS can provide a new approach for structure manipulation and performance enhancement of PSF membranes.     

Effect of Diluent Mixture on Porous Structure of Polyphenylene Sulfide via Thermally Induced Phase Separation

Polyphenylene sulfide (PPS) microporous membranes were prepared via the thermally induced phase separation process using diluent mixtures of diphenyl ether (DPE) and diphenyl ketone (DPK). The effects of DPE ratio to DPK in the diluent mixture on the microstructure were investigated. The results showed that the pore morphology of the membranes prepared from the diluent mixture was different from those of fabricated from pure diluents. Moreover, the pore structures of the membranes were changed along with the variation of the diluent composition.     

Construction of Renewable Superhydrophobic Surfaces via Thermally Induced Phase Separation and Mechanical Peeling

We report a simple preparation method of a renewable superhydrophobic surface by ther-mally induced phase separation (TIPS) and mechanical peeling. Porous polyvinylidene fluo-ride (PVDF) membranes with hierarchical structures were prepared by a TIPS process under different cooling conditions, which were confirmed by scanning electron microscopy and mer-cury intrusion porosimetry. After peeling off the top layer, rough structures with hundreds of nanometers to several microns were obtained. A digital microscopy determines that the surface roughness of peeled PVDF membranes is much higher than that of the original PVDF membrane, which is important to obtain the superhydrophobicity. Water contact angle and sliding angle measurements demonstrate that the peeled membrane surfaces display super-hydrophobicity with a high contact angle (152°) and a low sliding angle (7.2°). Moreover, the superhydrophobicity can be easily recovered for many times by a simple mechanical peel-ing, identical to the original superhydrophobicity. This simple preparation method is low cost, and suitable for large-scale industrialization, which may offer more opportunities for practical applications.