磺化聚醚酰亚胺/聚醚酰亚胺共混膜的结构与性能

将亲水性的磺化聚醚酰亚胺(SPEI)和疏水性的聚醚酰亚胺(PEI)共混,以N,N-二甲基乙酰胺(DMAc)为溶剂,制备了SPEI(Na型)／SPEI中空纤维超滤膜．研究了纺丝过程中内凝固浴组成比例和空气间隙距离变化对膜结构以及膜分离性能的影响。实验结果表明,随着内凝固浴中DMAc含量的提高,纤维内指状孔减少,水通量下降,而截留率则不受影响;随着空气间隙距离的增大,从膜内壁侧出发的指状孔结构前端逐渐向外壁发展,而膜的外壁侧则逐渐变得致密,同时,膜的外表面可能出现较大的微孔结构,导致膜的水通量随着空气间隙距离的增加而迅速增加后随之下降,而截留率则一直保持下降趋势。     

单醚二酐型聚醚酰亚胺的透气性能与分子结构之间关系的研究

合成了一系列单醚二酐型聚醚酞亚胺（ＰＥＩ），研究了它们对Ｈ２、ＣＯ２、Ｏ２、Ｎ２和ＣＨ４５种气体的透过性能与分子结构的关系．结果表明，这类聚醚欧亚胺的分子结构对其透气性和透气选择性有很大的影响，聚合物的自由体积和链段活动性是控制透气性和透气选择性的主要因素．二苯醚四酸二酐（ＯＤＰＡ－４．４＇－二Ｊ氨基二苯异丙烷（ＩＰＤＡ）具有很大的自由体积和较小的链段活动性、很大的透气性和较小的透气选择性，ＯＤＰＡ—４，４’－二氨基二苯酮（ＤＡＢＰ）具有很小的自由体积和较小的链段活动性、很小的透气性和较大的透气选择性，ＯＤＰＡ—３，３’－二甲基二苯甲烷二胶（ＤＭＭＤＡ）具有较大的自由体积和较小的链段活动性、很大的透气性和很大的透气选择性．     

双醚二酐型聚醚酰亚胺的透气性能与分子结构之间关系的研究Ⅰ

合成了一系列双醚二酐型聚醚酰亚胺（ＰＥＩ），研究了它们对Ｈ２、ＣＯ２、Ｏ２、Ｎ２和ＣＨ４五种气体的透过性能与分子结构的关系．结果表明，这类聚醚酰亚胺的分子结构对其透气性和透气选择性有很大的影响，聚合物的自由体积和链段活动性是控制透气性和透气选择性的主要因素。三种带有酰亚胺键邻位取代基的聚醚酰亚胺（ＨＱＤＥＡ—ＤＭｏＢＤＡ、ＨＱＤＥＡ—ＤＭＭＤＡ和ＨＱＤＥＡ—ＤＭｏＭＤＡ）具有较大的自由体积和较小的链段活动性、很高的透气性和透气选择性。     

一种新型含萘聚醚酰亚胺的合成与表征

本文合成了一种新型含萘酰亚胺六元环结构的双氯单体BCNPI, 然后将其与双酚A双钠盐在环丁砜中高温缩聚, 得到一种新型含萘聚醚酰亚胺, 并对其基本性能进行表征.     

聚四氟乙烯和石墨对聚醚酰亚胺摩擦学性能的影响

将聚四氟乙烯(PTFE)和石墨两类减摩耐磨填料填充到聚醚酰亚胺(PEI)中,表征其摩擦性能,利用扫描电子显微镜分析了磨损表面的显微结构,并分析了磨损机制.研究结果表明,PTFE和石墨的填充明显改善了PEI的摩擦磨损性,摩擦系数降低到0.3以下(纯PEI的摩擦系数为0.41),磨损率降低了3个数量级.在PTFE体系中,PTFE质量分数为10%时,PEI基共混材料的摩擦系数最低为0.23;而在质量分数为15%的石墨体系中,PEI基共混材料摩擦系数最低为0.27.磨损率随着填料含量的增加而逐渐下降,在填料质量分数为20%之后,摩损率下降平缓.因此PTFE和石墨的填充对PEI的摩擦学性能起到了很好的改善作用,而且PTFE比石墨的改善效果更优益.共混物的机械性能测试结果表明,在填料质量分数为5%~15%时,共混物具有良好的机械性能.     

聚萘酰亚胺膜的制备及其气体分离性能

利用萘二酐与邻位含脂肪族取代基的芳香二胺聚合制备了一系列均聚及共聚萘酰亚胺。这些C—N键邻位含取代基的聚萘酰亚胺可溶解于有机溶剂中并具有良好的成膜性。这些膜的拉伸强度在54~77 MPa之间,断裂伸长率在6.4%~8.1%,杨氏模量在1.3~2.2 GPa。这些聚萘酰亚胺具有优异的热稳定性,热分解温度在448~501℃范围内,玻璃化转变温度在382~391℃范围内。气体分离性能测试结果表明,聚萘酰亚胺具有突出的CO_2/CH_4分离能力,CO_2气体透过系数在37.2~151 barrer范围内,而CO_2/CH_4的选择系数在20.9~31.7的范围内,这表明了制备的聚萘酰亚胺气体分离膜材料在天然气纯化方面具有潜在的应用价值。     

热塑性聚醚酰亚胺改性四官能度环氧树脂的相分离研究Ⅳ.聚醚酰亚胺用量的影响

研究了不同用量新型苯端基聚醚酰亚胺（Ｐ－ＰＥＩ）对其改性４,４’－二氨基二苯甲烷四缩水甘油醚环氧树脂（ＴＧＤＤＭ）／４,４’－二氨基二苯砜（ＤＤＳ）体系的固化速率及相结构的影响。结果表明,随着ＰＥＩ用量的增加,固化反应速率增大,形成了不同的相结构。解释了ＰＥＩ用量对粘接剪切强度的影响。     

磺化聚醚酰亚胺/聚醚砜共混型质子交换膜的制备及其性能

以磺化聚醚酰亚胺(SPEI)和聚醚砜(PES)为原料, 采用溶液共混法成功制备出了SPEI/PES共混型质子交换膜,并经热重分析、AFM、SEM等对膜的结构和性能进行了表征. 结果表明, 共混膜较纯SPEI膜具有更高的热稳定性和较低的溶胀性; 在室温环境下, 共混膜在干态和湿态时均具有优异的机械性能; 与纯SPEI膜相比, 共混膜的形态结构更为致密, 这将有利于降低甲醇的渗透性. 采用交流阻抗法和隔膜扩散法分别考察了膜的质子传导性和阻醇性能, 对于共混质量比为50/50的膜来说, 其质子传导率达到了5.5 mS·cm-1的水平, 能满足质子交换膜的需求, 但其甲醇渗透系数明显降低, 仅为市用Nafion 112膜的5%, 这表明该共混膜有望作为一种新型的直接甲醇燃料电池用质子交换膜.     

含有聚醚链段的可溶性聚酰亚胺气体分离膜材料及其性能

将4,4'-六氟亚异丙基-邻苯二甲酸酐(6FDA)和1,3-苯二胺(mPDA)与二端氨基聚醚缩聚, 得到含有聚醚柔性链段的聚酰亚胺气体分离膜材料. 所合成的共聚聚酰亚胺在N-甲基吡咯烷酮(NMP)和四氢呋喃(THF)等有机溶剂中具有良好的溶解性能. 研究了O2, N2, H2, CH4和CO2在聚酰亚胺均质膜中的渗透性能, 考察了二端氨基聚醚的含量、链长和化学结构对气体渗透性能的影响. 结果表明, 聚醚链段的引入增大了气体的扩散系数, 气体的渗透系数显著增大; 聚醚链段与CO2相对较强的相互作用, 增大了对CO2/N2的溶解选择性, CO2/N2的分离性能优于CO2/CH4, 同时CO2比H2优先透过膜.     

含聚醚链段聚酰亚胺膜的制备及气体分离性能

利用均苯四甲酸二酐（PMDA）与4,4’-二氨基二苯醚（ODA）和聚醚胺（PPO, Mn～2000）共聚合,合成聚酰胺酸前驱体,经热处理得到一系列含PPO链段的聚酰亚胺薄膜.研究了PPO链段的引入对薄膜结构及气体分离性能的影响.结果表明,在芳香族聚酰亚胺中引入柔性链段PPO有利于气体分子的传输.得益于PPO链段在分离膜内部形成的微相分离结构,气体分子在分离膜内的扩散系数随PPO含量的增加显著提升.当PPO含量为65 wt%时,PPO链段在分离膜内仍呈现非晶相,CO₂渗透系数高达131.61 Barrer,比PMDA/ODA均聚聚酰亚胺薄膜提高22倍.同时,得益于聚醚链段对CO₂独特的亲和作用,随着PPO含量的提高,分离膜对CO₂/N₂的分离系数由18.77提高至30.12.结果表明PPO链段的引入对于调控聚酰亚胺膜的结构和气体分离性能具有重要作用.     

分子结构对聚芳醚酮薄膜透气性的影响

分子结构对聚芳醚酮薄膜透气性的影响王忠刚，陈天禄，徐纪平（中国科学院长春应用化学研究所长春１３００２２）关键词聚芳醚酮，气体分离膜，结构－性能关系为了改善聚合物薄膜的透气性能，开发具有高透气性和高选择性的膜材料，人们对膜分子结构与透气性能间的关系进行...     

几种Cardo聚芳醚砜膜的气体透过行为

几种Ｃａｒｄｏ聚芳醚砜膜的气体透过行为王忠刚，陈天禄，徐纪平（中国科学院长春应用化学研究所长春１３００２２）关键词Ｃａｒｄｏ聚芳醚砜，膜，气体分离近年来的研究结果表明：同时增加聚合物的自由体积和限制分子链的链段活动性可以同时改善聚合物的气体透过系数和...     

由聚合物结构预测气体的透过性能

本文利用基团加和法,对20多种常见聚合物的自由体积和内聚能进行了计算。发现氧气和氮气在聚合物膜中的透过率与自由体积和内聚能的比值有直接关系。此比值越大,气体的透过率越大,透过率的对数与自由体积和内聚能的比值基本呈线性关系。据此,对未知聚合物可根据其化学结构,从已有的基团数据计算该比值,从而预测它对氧气和氮气的透过性能。     

微孔PI气体分离膜的研究进展

自具微孔材料(PIMs)由于自身刚性分子链的扭曲折叠等会产生高比表面积的微孔结构,相应的膜材料具有优异的气体分离性能。将刚性扭曲的结构单元引入到聚酰亚胺(PI)主链中就得到自具微孔PI。微孔型PI是近年来发展的一种新型PI,其微孔结构使得PI膜的气体分离性能得到很大提升,其中气体渗透系数的提升尤为显著,且保持了传统PI良好的热稳定性、化学稳定性及高力学强度等性质。本文重点介绍了微孔PI以及基于微孔PI复合膜的最新研究进展,并对其未来发展趋势进行了展望。     

Sulfonated Polyetherimide and Its Membranes

Polyetherimide(PEI) was sulfonated by chlorosulfonic acid for the first time. The sulfonated products were characterized by FT-IR, DSC, ion exchange capacity and water sorption measurement. The hydrophilicity of PEI was improved by the sulfonation. The PEI was blended with the sodium salt from of sulfonated PEI(SPEI) to prepare microporous membranes. The morphologies of the membranes were studied with Scanning Electron Microscope (SEM).     

二维材料膜在气体分离领域的最新研究进展

Two-dimensional (2D) materials, led by graphene, have emerged as nano-building blocks to develop high-performance membranes. The atom-level thickness of nanosheets makes a membrane as thin as possible, thereby minimizing the transport resistance and maximizing the permeation flux. Meanwhile, the sieving channels can be precisely manipulated within sub-nanometer size for molecular separation, such as gas separation. For instance, graphene oxide (GO) channels with an interlayer height of about 0.4 nm assembled by external forces exhibited excellent H₂/CO₂ sieving performance compared to commercial membranes. Cross-linking was also employed to fabricate ultrathin (< 20 nm) GO-facilitated transport membranes for efficient CO₂ capture. A borate-crosslinked membrane exhibited a high CO₂ permeance of 650 GPU (gas permeation unit), and a CO₂/CH₄ selectivity of 75, which is currently the best performance reported for GO-based composite membranes. The CO₂-facilitated transport membrane with piperazine as the carrier also exhibited excellent separation performance under simulated flue gas conditions with CO₂ permeance of 1020 GPU and CO₂/N₂ selectivity as high as 680. In addition, metal-organic frameworks (MOFs) with layered structures, if successfully exfoliated, can serve as diverse sources for MOF nanosheets that can be fabricated into high-performance membranes. It is challenging to maintain the structural and morphological integrity of nanosheets. Poly[Zn₂(benzimidazole)₄] (Zn₂(bim)₄) was firstly exfoliated into 1-nm-thick nanosheets and assembled into ultrathin membranes possessing both high permeance and excellent molecular sieving properties for H₂/CO₂ separation. Interestingly, reversed thermo-switchable molecular sieving was also demonstrated in membranes composed of 2D MOF nanosheets. Besides, researchers employed layered double hydroxides (LDHs) to prepare molecular-sieving membranes via in situ growth, and the as-prepared membranes showed a remarkable selectivity of ~80 for H₂-CH₄ mixture. They concluded that the amount of CO₂ in the precursor solution contributed to LDH membranes with various preferred orientations and thicknesses. Apart from these 2D materials, MXenes also show great potential in selective gas permeation. Lamellar stacked MXene membranes with aligned and regular sub-nanometer channels exhibited excellent gas separation performance. Moreover, our ultrathin (20 nm) MXene nanofilms showed outstanding molecular sieving property for the preferential transport of H₂, with H₂ permeance as high as 1584 GPU and H₂/CO₂ selectivity of 27. The originally H₂-selective MXene membranes could be transformed into membranes selectively permeating CO₂ by chemical tuning of the MXene nanochannels. This paper briefly reviews the latest groundbreaking studies in 2D-material membranes for gas separation, with a focus on sub-nanometer 2D channels, exfoliation of 2D nanosheets with structural integrity, and tunable gas transport property. Challenges, in terms of the mass production of 2D nanosheets, scale-up of lab-level membranes and a thorough understanding of the transport mechanism, and the potential of 2D-material membranes for wide implementation are briefly discussed.     

Gas Permeation Properties of Organic-Inorganic Hybrid Membranes Prepared from Hydroxyl-Terminated Polyether and 3-isocyanatopropyltriethoxysilane

Organic-inorganic hybrid materials were prepared by reacting 3-isocyanatopropyltriethoxysilane (IPTS) with hydroxyl terminated poly(ethylene glycol) (PEG), poly(propylene glycol) (PPG) and poly(propylene glycol)-block-poly(ethylene glycol)-block-poly(propylene glycol) (PEPG), followed by hydrolysis and condensation with acid catalysis. Composite membranes have been obtained by casting hybrid sol on the microporous polysulfone substrate. The membranes were characterized by Fourier transform infrared (FT-IR), ¹³C NMR and ²⁹Si NMR. The permeability coefficients of N₂, O₂, CH₄ and CO₂ were measured by variable volume method. The gas permeability coefficients increase with increasing molecular weight of the polyethers. For the membranes containing PEG and PEPG, the higher values of CO₂ permeability coefficients and CO₂/N₂ separation factors are due to the presence of ethylene oxide segments. In case of PEPG membranes, molecular weight has more influence on CO₂ permeability than the effect of facilitation by ethylene oxide. The addition of TEOS into hybrid sol results in the decrease of all the gas permeability and does not affect the gas selectivity. PEG2000 membrane display the most performance among the hybrid membranes investigated here. The best values observed are CO₂ permeability of 94.2 Barrer with selectivity of 38.3 for CO₂/N₂ and 15.6 for CO₂/CH₄.