聚酰胺酸湿法纺丝凝固过程三元相图的初步构建

利用浊点滴定法构建了聚酰胺酸(PAA)/N,N-二甲基乙酰胺(DMAc)/水(H2O)体系的三元相图.研究了PAA的特性黏数和分子结构变化对三元相图的影响.结果表明,PAA/DMAc/H2O三元体系只发生液-液相分离;相转变时体系的组成配比存在线性关系.在一定范围内,PAA特性黏数的变化基本不影响体系三元相图的构成.不同分子结构PAA的三元体系,其相分离过程对温度的敏感程度不同.     

熔融纺丝制备中空纤维膜研究进展

中空纤维膜作为一种重要的分离膜材料,其制备方法一直以来是膜技术研究领域的热点。相对于溶液法纺丝制膜方法而言,熔融纺丝法具有使用溶剂量少、环境友好、所得中空纤维膜力学性能较优等特点,已成为目前中空纤维膜制备的重要技术之一。本文根据工艺将熔融纺丝制膜方法区分为熔融纺丝-拉伸法和热致相分离法,分别就这两种方法中空纤维膜的制备技术及致孔机理进行介绍,并对二者的研究历史及现状进行了论述,最后,还指出了熔融纺丝制备中空纤维膜研究领域有待解决的问题。     

内凝固浴组成对聚醚酰亚胺中空纤维膜结构和性能的影响

以N,N-二甲基乙酰胺(DMAc)为溶剂,水为外凝固浴,乙醇为内凝固浴,DMAc为内凝固浴添加剂,采用相转化法制备了聚醚酰亚胺(PEI)中空纤维膜,研究了内凝固浴组成和纺丝液浓度对膜结构和性能的影响。实验结果表明,随着内凝固浴中DMAc含量在一定范围内增加,纤维断面指状孔有所减少,内表面由无孔到有微孔出现,但膜的水通量下降,截留率不受影响;随着纺丝液浓度提高,膜的水通量下降,截留率提高。     

制膜液黏度对单皮层PVDF中空纤维膜纺制的影响

以二甲基乙酰胺(DMAc)为溶剂,制备聚偏氟乙烯(PVDF)浓度为15%的制膜液,考察了DMAc同时作为内凝胶浴时膜结构的变化.为保持纺膜过程中的稳定性,分别考察了添加剂LiCl、水以及表面活性剂对制膜液黏度的影响.实验发现添加LiCl可以大大提高制膜液的黏度,而水作为添加剂时对黏度的影响与制膜液本身的浓度有关.在不提高制膜液浓度的基础上,通过提高制膜液黏度克服了膜在纺制过程中的不稳定问题,得到阻力较小的,指状孔贯穿的单外皮层中空纤维膜.     

纳米纤维增强双层组织引导膜的力学性能及细胞响应

通过热致相分离结合静电纺丝技术,在纳米羟基磷灰石/聚酰胺(n HA/PA)多孔膜基底表面形成不同取向的PA纳米纤维,制备了纤维增强双层组织引导膜.研究了不同转速(0,500,1500 r/min)下,n HA/PA多孔膜表面形成的PA纳米纤维的微观结构及取向情况对力学性能的影响.将双层组织引导膜与MG63细胞共培养,研究细胞在双层组织引导膜周围的生长情况,并通过四甲基偶氮唑盐比色法(MTT)定量研究了细胞的增殖情况.结果表明,热致相分离法制备的n HA/PA多孔膜表面及内部富含多孔结构,n HA晶粒在PA基质中均匀分布.采用静电纺丝法在n HA/PA多孔膜表面构建纳米纤维,随着转速增大,n HA/PA多孔膜表面的PA纳米纤维取向性逐渐增加.引入PA纳米纤维后,双层组织引导膜的力学性能均有增强,在500 r/min转速下,双层组织引导膜中,纳米纤维层与n HA/PA基底应变同时达到最大,拉伸强度达到(39.86±4.73)MPa.细胞实验结果显示,双层组织引导膜周围的细胞生长良好,增殖明显,具有良好的细胞相容性,在牙周组织缺损再生领域有潜在应用前景.     

界面预湿处理对异质增强型PVDF中空纤维膜结构与性能的影响

以熔融纺丝聚氯乙烯(PVC)中空纤维多孔膜为增强体,聚偏氟乙烯(PVDF)为成膜聚合物,聚乙烯吡咯烷酮(PVP)为添加剂,N,N-二甲基乙酰胺(DMAc)为溶剂,配置铸膜液,采用同心圆牵引-涂覆法制备了异质增强型PVDF中空纤维膜.制备过程中,采用预湿溶液对增强体基膜表面进行预处理,研究了预湿溶液组成及含量对异质增强型PVDF中空纤维膜结构与性能的影响.结果表明,未经预湿处理的异质增强型PVDF中空纤维膜具有较厚的致密界面层;预湿溶液可对基膜表面孔起到保护作用,使异质增强型PVDF中空纤维膜的界面层变薄或形成多孔界面层,有益于改善增强型PVDF中空纤维膜的通透性能;与二甲基乙酰胺(DMAc)水溶液相比,以乙醇水溶液为预湿溶液所得异质增强型PVDF中空纤维膜的性能较优;当预湿液中乙醇含量为60 wt%时,所得增强型PVDF中空纤维膜的渗透性能较优,拉伸强度可达8.61 MPa.     

非溶剂添加剂对共聚砜铸膜液体系及膜性能与结构的影响

以含二氮杂萘酮结构的新型共聚砜为膜材料 ,通过浊点滴定法和特性粘数的测定研究了几种非溶剂添加剂对铸膜液体系的影响 .并由共聚砜 NMP 添加剂三组分相分离曲线数据计算了共聚砜的Θ溶剂中NMP与添加剂的比例 ,考察了添加剂EGME用量对共聚砜超滤膜结构和性能的影响 .发现当EGME NMP接近Θ组成时膜性能发生突变 ,在EGME NMP低于Θ组成时 ,膜的水通量随添加剂用量的增大而增大 ,截留率基本不变 .     

Armos/聚砜共混中空纤维基膜及其纳滤复合膜的制备与性能研究

中空纤维膜因其体积装填密度高、占地面积小、成本相对低等优点备受关注。本文通过将Armos聚合液与聚砜(PSf)共混，经干-湿法纺丝制备了Armos/PSf共混中空纤维超滤膜，研究表明：Armos均匀分散在中空纤维膜中，中空纤维膜断面呈现疏松的多孔结构，随着Armos共混含量的增加，膜的亲水性和纯水通量均提高，但对PEG-20000截留率下降明显。以Armos/PSf共混中空纤维膜为基膜，通过界面聚合制备了中空纤维复合纳滤膜，优化的制备条件为：基膜中Armos的共混含量为4%、水相单体浓度为3%、油相单体浓度为0.15%时，制得的中空纤维复合纳滤膜性能最佳，其通量为8.40L/(m²·h)，对MgSO₄的截留率为88%。     

TEP-DMAc混合溶剂对PVDF膜性能的影响

利用非溶剂相转化法(NIPS)制备聚偏氟乙烯(PVDF)膜,考察了聚乙二醇(PEG200)与N,N-二甲基乙酰胺(DMAc)的质量比对膜分相速率和膜性能的影响,讨论了以磷酸三乙酯(TEP)和DMAc的混合液作溶剂对PVDF膜凝胶速率、膜结构和膜通量的影响。结果表明:PEG200的加入减弱了溶剂对聚合物的溶解能力,但铸膜液的分相行为由延迟分相转变为瞬时分相,膜通量提高。随着混合溶剂中TEP含量的增大,铸膜液的黏度增大,分相速率减慢;在高质量比m(TEP)/m(DMAc)时,膜表面的孔增多,指状孔膜结构逐渐消失,整个膜截面呈海绵状,膜通量变大,力学性能提高。     

纤维编织管增强型中空纤维膜研究

采用二维编织技术将聚丙烯腈(PAN)长丝编织成中空纤维编织管作为增强体,分别以聚丙烯腈(PAN)和聚偏氟乙烯(PVDF)为成膜聚合物,N,N-二甲基乙酰胺(DMAc)为溶剂,聚乙烯吡咯烷酮(PVP)为添加剂,调制铸膜液,采用同心圆挤出-涂覆法制备了PAN纤维编织管同质增强型PAN中空纤维膜和异质增强型PVDF中空纤维膜.研究表明,所得PAN纤维编织管增强型中空纤维膜断裂强度最大可超过75 MPa,在伸长率10%范围内,表面分离层与增强体之间界面结合良好;表面分离层具有类似于非对称膜的结构,铸膜液可浸入纤维编织管纤维空隙中,铸膜液浸入部分固化后未影响膜的通透性能;随成膜聚合物浓度增加,膜纯水通量减小,牛血清白蛋白(BSA)截留率增大;随添加剂PVP浓度增加,膜的纯水通量先增大后减小,在8 wt%左右达最大值,BSA截留率随PVP浓度增加而单调增加;同质增强型中空纤维膜界面结合程度优于异质增强型.     

Effect of solution extrusion rate on morphology and performance of polyvinylidene fluoride hollow fiber membranes using polyvinyl pyrrolidone as an additive

<正>Polyvinylidene fluoride(PVDF) hollow fiber membranes prepared from spinning solutions with different polyvinyl pyrrolidone(PVP) contents(1%and 5%) at different extrusion rates were obtained by wet/dry phase process keeping all other spinning parameters constant.In spinning these PVDF hollow fibers,dimethylacetamide(DMAc) and PVP were used as a solvent and an additive,respectively.Water was used as the inner coagulant.Dimethylformamide(DMF) and water(30/70) were used as the external coagulant.The performances of membranes were characterized in terms of water flux,solute rejection for the wet membranes.The structure and morphology of PVDF hollow fiber were examined by BET adsorption,dry/wet weight method and scanning electron microscopy(SEM).It is found that the increase in PVP content and extrusion rate of spinning solution can result in the increase of water flux and decrease of solute rejection.The improvements of interconnected porous structure and pore size are induced by shear-thinning behavior of spinning solution at high extrusion rates,which could result in the increase of water flux of hollow fiber membranes.The increase of extrusion rate also leads to the increase of membrane thickness due to the recovery effect of elastic property of polymer chains.     

ULTRAFILTRATION MEMBRANE FORMATION OF PES-C, PES AND PPESK POLYMERS WITH DIFFERENT SOLVENTS

Ultrafiltration membranes were prepared using phenolphthalein polyarylethersulfone (PES-C),polyethersulfone (PES) and poly(phthalazinone ether sulfone ketone) (PPESK) as polymers and NMP,DMAc,DMF and DMSO as solvents by immersion precipitation via phase inversion.Experimental data of thermodynamic properties of the polymer solutions and kinetic process of membrane formation were reported.For polymer solutions with good solvents,the sequence of the viscous flow activation energy (E_η) was coincident with ...     

添加剂对PVDF相转化过程及膜孔结构的影响

研究了PVP、PEG及LiCl 3种成孔添加剂下PVDF DMAc H2 O 添加剂体系的成膜机理 .无论那种添加剂的铸膜液相转换成膜过程中都存在凝胶分相和液液分相两种相变方式 ,在 30～ 6 0℃时凝胶分相在较低的非溶剂浓度下先于液液分相发生 ,LiCl作为添加剂较PEG、PVP对铸膜液有较强的致凝胶作用 ,成膜过程中凝胶分相段时间依PVP、PEG、LiCl的顺序延长 ,导致液液分相初始分相点处聚合物浓度增大 ,阻止了大孔结构的充分发展 .制得的膜依PVP、PEG、LiCl的顺序有效孔隙率和通量降低 ,结晶度升高 .以LiCl为添加剂制得的膜几乎不改变PVDF膜的疏水性 ,而以PVP或PEG为添加剂的膜隔水压差降低约 2 0kPa .     

Synthesis of polypiperazine-amide thin-film membrane on PPESK hollow fiber UF membrane

A new interfacial polymerization (IP) procedure is developed in order to synthesize polypiperazine-amide thin-film membrane on the inner surface of poly(phthalazinone ether sulfone ketone) (PPESK) hollow fiber ultrafiltration (UF) membrane.A hollow fiber composite membrane with good performance was prepared and studied by FT-IR and scanning electron microscopy.     

Preparation and characterization of asymmetric polyethersulfone (PES) membranes

Flat‐sheet asymmetric polyethersulfone (PES) membranes were prepared from polyethersulfone (PES)/ polyethylene glycol (PEG)/ N‐methyl‐2‐pyrrolidone (NMP) system via phase inversion induced by immersion precipitation in water coagulation bath. Effects of propionic acid (PA) as a non‐solvent additive (NSA) on morphology and performance of the membranes prepared from PES/PEG 6000/NMP system in water coagulation bath were investigated. The cross section morphology of the membranes was studied by scanning electron microscopy (SEM). In addition, performance of the membranes was studied by water content measurements and separation experiments using pure water and human serum albumin (HSA) protein solution as feeds. According to SEM analysis, it was found out that the NSA has a significant influence on the structure of the skin layer and the sublayer. The obtained results indicated that addition of PA to the casting solution decreases permeation flux of the prepared membranes. Copyright © 2009 John Wiley & Sons, Ltd.     

Preparation and characterization of polyvinylidene fluoride (PVDF) hollow fiber membranes

Polyvinylidene fluoride (PVDF) hollow fiber membranes were prepared by dry/wet and wet phase inversion methods. In spinning these PVDF hollow fibers, dimethylacetamide (DMAc) and polyvinyl pyrrolidone (PVP) were used as a solvent and an additive, respectively. Water was used as the external coagulant. Water or ethanol was used as the internal coagulants. The membranes were characterized in terms of water flux, molecular weight cut-off for the wet membranes. Gas permeation fluxes and effective surface porosity were determined by a gas permeation method for the dried membranes. The cross-sectional structures were examined by scanning electron microscopy. The effects of polymer concentration, air-gap, PVP molecular weight, PVP content in the polymer dope, and the internal coagulant on the permeation properties and membrane structures were examined. Highly permeable PVDF hollow fiber membranes could be prepared from a polymer dope containing low molecular weight PVP and using ethanol as the internal coagulant.     

PREPARATION OF ASYMMETRIC POLYETHERKETONE FLAT AND HOLLOW FIBER MEMBRANES FOR GAS SEPARATION USING ACETIC ACID BASED COAGULANTS

Membranes for gas separation have developed significantly in the last twenty years,however,there is still a need for high temperature and chemically resistant membranes that exhibit good selectivity and gas permeability.Our study examines the fundamental properties of polyetherketone (PEK,a thermally stable and chemically resistant polymer) membranes prepared using concentrated sulphuric acid (98% H_2SO_4) as the solvent.Non-solvents used in the work included acetic acid,ethanol,methanol,glycerol,and wat...     

The effects of flow angle and shear rate within the spinneret on the separation performance of poly(ethersulfone) (PES) ultrafiltration hollow fiber membranes

The effects of dope flow rate and flow angle within a spinneret during spinning hollow fiber membranes on the morphology, water permeability and separation performance of poly(ethersulfone) ultrafiltration hollow fiber membranes were investigated. For this purpose, two spinnerets with different flow angles were designed and used. The dope solution, containing polyethersulphone (PES)/N-methyl-2-pyrrolidone (NMP)/diethylene glycol (DG) with a weight ratio of 23/41/36, which was very close to its cloud point (binodal line), was used in order to speed up the coagulation of nascent fibers so that the relaxation effect on molecular orientation was reduced. The wet-spinning process was purposely chosen to fabricate the hollow fibers without extra drawing. Therefore, the effects of gravity and elongation stress on fiber formation could be significantly reduced and the orientation induced by shear stress within the spinneret could be frozen into the wet-spun fibers. Experimental results suggest that higher dope flow rates (shear rates) in the spinneret produce UF hollow fiber membranes with smaller pore sizes and denser skin layers due to the enhanced molecular orientation. Hence, the pore size and the water permeability decrease, but the solute separation increases. Hollow fibers spun from a conical spinneret have smaller mean pore sizes with larger geometric standard deviations, thus exhibiting lower water flux and greater solute separation than hollow fibers spun from a traditional straight spinneret. In addition, SEM studies indicate macrovoids response differently for the 90° straight and 60° conical spinnerets when increasing the dope flow rate. Macrovoids can be significantly suppressed and almost disappear in the 90° spinneret at high dope flow rates. This phenomenon cannot be observed for the 60° conic spinneret.     

STRUCTURE AND PROPERTIES OF COMPOSITE POLYURETHANE HOLLOW FIBER MEMBRANES

Composite polyurethane (PU)-SiO2 hollow fiber membranes were successfully prepared via optimizing the technique of dry-jet wet spinning, and their pressure-responsibilities were confirmed by the relationships of pure water fluxtransmembrane pressure (PWF-TP) for the first time. The origin for this phenomenon was analyzed on the basis of membrane structure and material characteristics. The effects of SiO2 content on the structure and properties of membrane were investigated. The experimental results indicated that SiO2 in membrane created a great many interfacial micro-voids and played an important role in pressure-responsibility, PWF and rejection of membrane: with the increase of SiO2 content, the ability of membrane recovery weakened, PWF increased, and rejection decreased slightly.