共混改性聚酰亚胺中空纤维膜的压缩空气除湿性能研究

采用干／湿相转换法制备了共混聚酰亚胺中空纤维膜,并对其与聚酢亚胺(PI)中空纤维膜的除湿性能进行了比较,结果表明：在不同压力、不同流量和不同吹扫比例的情况下,共混膜的除湿性能均优于PI膜,特别是增大吹扫比例时,共混膜的优越性更为明显,虽然在抽真空的条件下,共混膜的除湿性能不如采用吹扫操作方式的,但是,同PI膜相比脱湿性能仍然好于PI膜。     

聚联苯酰亚胺/聚硫醚酰亚胺共混体系的相容性

<正> 聚酰亚胺是一种性能极其优异的高性能树脂,它在许多高技术领域有着极其重要的应用价值。在80年代以前,人们工作的重点是合成出一系列分子结构不同的聚酰亚胺,研究分子结构与性能间的关系,开发聚酰亚胺新品种。自80年代后期,有关高性能树脂聚酰亚胺共混物的研究日益引起人们的关注,其中有关不同分子结构的聚酰亚胺/聚酰亚胺共     

聚醚酰亚胺/酚酞型聚醚醚酮共混体系相容性的稀溶液粘度法研究

<正> 近年来,有关高性能树脂聚酰亚胺共混物的研究日益引起人们的关注。已经发现许多种分子结构不同的聚酰亚胺之间,聚酰亚胺与聚苯并咪唑,或聚醚醚酮能形成完全相容的共混体系,从而扩大了高性能树脂聚酰亚胺的应用范围。 酚酞型聚醚醚酮(PEK-C)是由我所研究开发出的一种新型的聚醚醚酮类高性能树脂,它具有良好的可溶性,优异的机械强度和加工流动性,已广泛应用于结构材料及复合材料的制备。为进一步扩大该树脂的应用范围,本实验室在PEK-C共混物的研究做了大量的工作。本工作研究了聚醚酰亚胺(PEI)/PEK-C共混体系的相容性。PEI和PEK-C的分子结构如下:     

MCM-41负载型过氧磷钨杂多酸季胺盐催化剂的制备和结构性能的考察

合成了以MCM-41为载体的过氧磷钨杂多酸季胺盐系列催化剂,并用XRD,FTIR,BET等方法测定了催化剂的体表结构.发现不同晶化时间合成的MCM-41具有不同的孔结构和比表面,负载过氧磷钨杂多酸季胺盐以后的催化剂对18醇催化氧化成18酸表现了不同的催化性能,与无载体的过氧磷钨杂多酸季胺盐催化剂相比显示了更高的活性和选择性.     

氰化金浸取液萃取机理研究

本文利用Fourier变换红外光谱 (FTIR)、放射性同位素示踪、激光光散射的实验等方法研究了有机相的溶液结构 ,初步提出季胺盐萃取金有机相中氰化金阴离子参与形成超分子结构 ,并且随着有机相中金浓度的增加 ,萃合物形成聚集体     

分光光度法测定角膜接触镜护理液中聚季胺盐-1含量

利用分光光度法测定角膜接触镜护理液中聚季胺盐-1的含量,探讨护理液中其它成分对测定结果的影响。聚季铵盐-l与镁离子、染料丽春红S反应生成不溶性复合物,通过测量染料丽春红S吸光度的降低对聚季铵盐-l进行定量分析。检测波长为513 nm,聚季胺盐-1的质量浓度(X)在1.2~14.5μg/m L内与吸光度(Y)线性良好,线性方程为Y=0.061 7X–0.122 1,r~2=0.998 1。测定结果的相对标准偏差为1.1%(n=6),日间重复性为1.6%。样品3水平加标回收率为92.5%~99.9%。该法操作简单,方法稳定且准确,可作为角膜接触镜护理液中有效成分聚季胺盐-1质量控制的方法之一。     

高介电常数石墨烯/聚酰亚胺复合材料的制备与性能

在原位聚合制备氧化石墨烯/聚酰亚胺复合材料的过程中,加入季铵盐表面活性剂,抑制氧化石墨烯在高温亚胺化时的聚集,同时将氧化石墨烯原位还原,获得高介电常数的石墨烯/聚酰亚胺复合材料.结果表明,采用四丁基溴化铵和四丁基碘化铵作为还原剂,利用原位化学还原方法所制备的石墨烯/聚酰亚胺复合材料的介电常数超过聚酰亚胺薄膜40倍以上,复合材料的热稳定性和机械性能也优于聚酰亚胺薄膜.热重分析结果表明,在复合材料高温亚胺化过程中,季铵盐发生热分解,未残留在复合材料中.     

新型高效原油破乳剂PNT-05的研制与应用

针对中原油田采油六厂二区原油破乳脱水过程中存在的脱水速度慢,乳化中间层厚等问题,通过分子结构设计手段,在非离子型破乳剂基础上,经酯化,在破乳剂分子中引入阳离子基团,合成出季胺盐阳离子型破乳剂PNT－05,利用季胺盐阳离子型破乳剂与助剂复配的方法室内解决了中原油田二区原油破乳脱水过程中顾在的问题,与油田现场用破乳剂相比,新的破乳剂体系脱水速度快,脱水效率高,使乳化中间层变薄或消失,同时探讨了季胺盐阳离子型破乳剂PNT－05的作用机制。     

聚酰亚胺改性酚醛泡沫

介绍了聚酰亚胺(PI)与酚醛树脂的共混改性方法,同时探讨了聚乙二醇(PEG)的加入对酚醛/聚酰亚胺复合体系的性能影响.结果显示经聚酰亚胺改性后,酚醛复合材料形成了网络互穿结构,其热稳定性、压缩强度以及隔热性能均有明显提高,粉化率、吸水率也有所降低,但仍然具有较高的脆性.在酚醛/聚酰亚胺复合体系中适当的加入聚乙二醇后,材料的脆性得到改善,然而其它性能如压缩强度、热稳定性和隔热性却比加入前有所降低.通过研究发现,为了改善酚醛泡沫塑料总体性能,聚酰亚胺和聚乙二醇的最佳用量均为3%～5%.     

乙炔基封端聚酰亚胺增韧改性的相结构

以双酚A二醚二酐(BPADA)和3乙-炔苯胺(APA)为原料,通过两步法合成一种热固性可交联的聚酰亚胺预聚体.将此预聚体分别与不同结构的热塑性聚酰亚胺(PI)共混,对其进行增韧改性,通过调控热塑性聚酰亚胺的质量分数,引入结构相似且含有更多柔性基团的热塑性聚酰亚胺(如含有醚键和对称甲基结构的二酐),得到了热固/热塑性聚酰亚胺复合膜.利用差示扫描量热仪(DSC)及扫描电镜(SEM)对该体系的相分离结构和相容性进行研究,并讨论其机械性能和热性能.结果表明,相分离结构使体系的机械性能得到改善,同时也保持了原有的优异热性能.     

Charged ultrafiltration membranes of polyacrylonitrile covalently binding amphiphilic quaternary ammonium group: effect of aliphatic hydrophobic groups on the filtration properties

Amphiphilic monomers of chloromethylstyrene derivative were synthesized and then copolymerized with acrylonitrile for the preparation of positively charged ultrafiltration membranes. Four types of the polyacrylonitrile charged membranes having quaternary ammonium group with trimethyl, dimethylbutyl, dimethyloctyl and dimethylstearyl groups were prepared by the phase-inversion method. The ultrafiltration properties of the charged membranes were measured by using dextran molecular probes at various NaCl concentrations. Then, the filtration behavior was compared in these charged membranes. For membranes with trimethyl and dimethylbutyl groups on the quaternary ammonium salt, the values of the molecular weight cutoff and the permeation rate of the solute solution increased when the salt concentration increased. However, for membranes having amphiphilic quaternary ammonium groups with octyl and stearyl aliphatic chains, the filtration properties did not change with the salt concentration. We concluded that a compact conformation of the amphiphilic polyionic segments in the membrane causes stable filtration properties.     

Highly hydrophobic microporous low‐density polyethylene hollow fiber membranes by melt‐extrusion coupled with salt‐leaching technique

Microporous and highly hydrophobic low‐density polyethylene (LDPE) hollow fiber membranes were successfully prepared via a solvent‐free method, combining melt‐extrusion, and salt‐leaching techniques. NaCl particles with particle size of 5–10 µm were mixed with LDPE pellets to produce a blend of 35, 40, 50, 60, 65 and 68 wt% of salt. A microporous structure was produced by leaching the salt particles from the hollow fiber matrix via immersion in water at 60°C. The fabricated membranes were then characterized in terms of morphology, porosity and pore size distribution, surface roughness, and hydrophobicity, as well as mechanical properties. The remarkable increase in the water contact angles from 98° for LDPE hollow fibers fabricated without the addition of salt (blank sample) to 130° for membranes fabricated with initial salt content of 68 wt% is mainly attributed to the rough surface structure, comprising a large number of micropapillas produced by removing the imbedded salt crystals. The increase in surface roughness and porosity of hollow fiber membranes with increasing initial salt content was confirmed by scanning electron microscope and atomic force microscopy. Copyright © 2013 John Wiley & Sons, Ltd.     

聚全氟乙丙烯中空纤维膜研究

以聚全氟乙丙烯(FEP)为成膜聚合物,复合无机粒子为成孔剂,邻苯二甲酸二辛酯(DOP)为稀释剂,采用熔融纺丝工艺制备得到FEP中空纤维膜.分析和讨论了不同成膜体系对FEP中空纤维膜热性能、动态力学性能和力学性能的影响,并对膜的纯水通量和孔径分布进行表征.用扫描电子显微镜(SEM)观察了膜的横断面和表面形貌.结果表明,所得FEP中空纤维膜为由溶出微孔和界面微孔组成的海绵状孔结构.随着成孔剂含量的增加,成孔剂在成膜体系中分散程度变差,容易发生团聚,最终导致膜孔径变大,孔径分布变宽.成孔剂和稀释剂对FEP中空纤维膜的热性能和动态力学性能影响较小.当FEP含量增加到70 wt％时,膜表面容易形成一层致密层,降低了膜的通透性.     

Poly(vinylidene fluoride)-graft-poly(N-vinyl-2-pyrrolidone) copolymers prepared via a RAFT-mediated process and their use in antifouling and antibacterial membranes

PNVP-g-PVDF copolymers were synthesized and used to produce microfiltration membranes. The pore size and distribution varied with the grafting concentration and the density of graft points. A significant decrease of the amounts of adsorbed BSA indicated improved antifouling properties of PVDF. The MF membranes were further functionalized via surface-initiated block copolymerization with DMAEMA to obtain (PVDF-g-PNVP)-b-PDMAEMA MF membranes. Quaternization of the tertiary amine groups of the PDMAEMA brushes gave rise to a high concentration of quaternary ammonium salt on the membrane surfaces. The bactericidal effect of the QAS-functionalized membranes on E. coli was also demonstrated and discussed.     

Fabrication of polymer/fluoride-containing salts blend composite membranes for CO_2 separation

Poly (N,N-dimethylaminoethyl methacrylate)-poly (ethylene glycol methyl ether methacrylate) (PDMAEMA-PEGMEMA) and cesium fluoride (CsF) were blended and used as the separation material of composite membranes.Hollow fiber composite membranes were fabricated by coating the blend on polysulfone (PSf) hollow fiber substrate.Introduction of fluorine ion improved the separation performance of the membrane.The concentration of coating solution was adjusted to obtain a membrane with high permeance.The composite membrane showed good performance with the CO2 permeance of 30.4 GPU (1 GPU=10-6 cm3 (STP)/(cm 2 s cmHg)),and selectivities to CO2/N2,CO2/CH4,CO2/H2 and O2/N2 of 47.2,37.6,1.75 and 4.70,respectively.Potassium fluoride (KF),due to its low cost,was also used as a substitute of CsF to prepare composite membrane and the permeation data showed that CsF can be replaced by KF.The effect of operating temperature on the permeation properties of the composite membrane was also investigated.     

木质素磺酸钠改性聚砜膜的制备及其在正渗透膜中的应用

采用木质素磺酸钠作为亲水添加剂,通过浸没沉淀相转化法制备了木质素磺酸钠共混改性聚砜膜,以改善聚砜膜的亲水性,并用作正渗透膜的支撑层,以降低内浓差极化效应.利用扫描电子显微镜、衰减全反射傅里叶变换红外光谱仪、水接触角仪等研究了不同木质素磺酸钠添加量对聚砜膜的结构和表面性质的影响.结果表明,添加木质素磺酸钠后,聚砜膜的指状孔变得规整且狭长.水接触角实验证实添加木质素磺酸钠能改善聚砜膜的亲水性,当木质素磺酸钠含量为0.4 wt%时,聚砜膜的表面水接触角可降低至65°.正/反渗透测试装置分别用于表征正渗透膜的传质性质和结构参数.结果表明,以0.4 wt%木质素磺酸钠改性聚砜膜为支撑层的正渗透膜的水渗透性能(A=3.12×10~(-5) LMH×Pa~(-1))优于纯聚砜基底正渗透膜(0.76×10~(-5)LMH×Pa~(-1)),而且前者的结构参数(S=2010mm)远小于后者(3450mm),说明木质素磺酸钠改性聚砜膜有效弱化了正渗透膜的内浓差极化效应.     

Polyamide-imide/polyetherimide dual-layer hollow fiber membranes for pervaporation dehydration of C1–C4 alcohols

To circumvent the common swelling and deteriorated performance of integral asymmetric hollow fiber membranes for pervaporation dehydration, we have developed novel polyamide-imide (PAI)/polyetherimide (PEI) hollow fiber membranes with synergized performance with the aid of dual-layer spinning technology. Dehydration of C1–C4 alcohols has been conducted and the orders of their fluxes and permeances have been analyzed. The hollow fibers spun at 2 cm air gap and annealed at 75 °C exhibit the highest pervaporation performance: separation factors for t-butanol/water and iso-butanol/water binary systems are greater than 50,000 with flux more than 700 g/m² h. A comparison with literature data shows that the newly developed membranes outperform most other polymeric membranes for the dehydration of IPA and butanols. The dual-layer hollow fiber membranes also exhibit good long-term stability up to 200 h. The superior performance can be attributed to (1) the balanced properties of PAI as the selective layer for dehydration pervaporation; (2) the low water uptake and less swelling characteristic of the PEI supporting layer; and (3) the desirable membrane morphology consisting of a fully porous inner layer, a porous interface, and an ultrathin dense-selective outer skin.     

Dehydration of acetic acid by pervaporation using SPEK-C/PVA blend membranes

Sulfonated cardo polyetherketone (SPEK-C) and poly(vinyl alcohol) (PVA) blend membranes were prepared by solution casting method and used in pervaporation (PV) dehydration of acetic acid. The membranes were characterized by Fourier transform infrared (FTIR), X-ray diffraction (XRD), scanning electron microscopy (SEM) and contact angle meter. The results show that thermal crosslinking occurred to the membrane under high temperature annealing. The effective d-spacing (inter-segmental spacing) decreased with PVA content decreasing. The hydrophilicity of the blend membrane increased with SPEK-C content increasing. Swelling and sorption experiments show that the swelling degree of the blend membrane increased, however both the sorption and diffusion selectivities decreased with increasing PVA content. The diffusion selectivity is higher than the sorption selectivity. This suggests that PV dehydration of acetic acid is dominated by the diffusion process. The pervaporation separation index (PSI) of the membrane increases with increasing PVA content and arrives at a maximum when the SPEK-C/PVA ratio is 3/2, then decreases with further addition of PVA. The membrane has an encouraging separation performance with a flux of 492 g m⁻² h⁻¹ and separation factor of 59.3 at 50 °C at the feed water content 10 wt%.     

Fabrication of polymer/fluoride-containing salts blend composite membranes for CO2 separation

Poly (N, N-dimethylaminoethyl methacrylate)-poly (ethylene glycol methyl ether methacrylate) (PDMAEMA-PEGMEMA) and cesium fluoride (CsF) were blended and used as the separation material of composite membranes. Hollow fiber composite membranes were fabricated by coating the blend on polysulfone (PSf) hollow fiber substrate. Introduction of fluorine ion improved the separation performance of the membrane. The concentration of coating solution was adjusted to obtain a membrane with high permeance. The composite membrane showed good performance with the CO2 permeance of 30.4 GPU (1 GPU = 10^-6 cm³(STP)/(cm²·s·cmHg)), and selectivities to CO2/N2, CO2/CH4, CO2/H2 and O2/N2 of 47.2, 37.6, 1.75 and 4.70, respectively. Potassium fluoride (KF), due to its low cost, was also used as a substitute of CsF to prepare composite membrane and the permeation data showed that CsF can be replaced by KF. The effect of operating temperature on the permeation properties of the composite membrane was also investigated.