富马酸二异丙酯—富马酸二正庚酯共聚物的合成与气体透过性能

自Bengough等用自由基引发聚合的方法首次得到了较高分子量的聚富马酸二乙酯后,有关富马酸酯(DRFs)类单体的聚合反应及其结构性能已进行了许多研究。结果表明,这类单体的聚合物在聚合反应活性、聚合物结构及性能等方面均有某些独特的性质,如聚富马酸二异丙酯(PDiPF)和聚富马酸二特丁酯(PDtBF)两种聚合物具有良好的氧氮透过性。我们曾研究十几种DRFs单体的聚合反应,得出非正烷基酯基的单体如富马酸二异丙酯(DiPF),富马     

三甲基硅烷基丙炔与五甲基二硅烷基丙炔共聚物膜及其气体透过性

研究了三甲基硅烷基丙块与五甲基二硅烷基丙块共聚物〔poly(TMSP-co-PMDSP)〕的成膜特点。poly(TMSP-co-PMDSP)膜的气体透过系数分别为:P_(O2):4×10~3～12×10~3,P_(N2):3×10~3～8×10~3和P_(CO2):2×10~4～4×10~4barrer,气体透过稳定性低,透过行为偏离第二Fick定律,过系数下降,其中溶解系数降低的比例远大于扩散系数的增加比例,在含有凝聚性气体的环境里,膜的气体透过出现表面吸附控制的特征。     

聚1—三甲硅基丙炔的改性及其氧氮透过性

80年代才研制的聚1-三甲硅基丙炔(PTMSP)的T_g高于200℃,而它在室温的气体透过性呈橡胶态聚合物的特性,透氧和透醇速率极高,Po_2达5×10~3Barrer,是一代新型富氧膜材料。但TMSP制备和聚合难度大。目前尚只有日、美等国取得一些进展,他们     

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。     

聚(4-三甲基硅基)苯乙炔膜的气体透过性

合成了4-三甲基硅基苯乙炔(SPA)单体,采用核磁共振谱(1H-NMR)和傅里叶变换红外光谱(FT-IR)对其进行了表征.在Pd(PPh3)2Cl2和金属共催化剂催化下制备了聚4-三甲基硅基苯乙炔(PSPA).PSPA易溶于氯仿、甲苯等有机溶剂,成膜性较好,具有较高的强度和热稳定性.热重分析(TGA)表明其5%失重温度为300～310℃.PSPA膜对CO2气体透过系数达到848 Barrer,并具有较高的透过选择性,分离系数达到12.68,摆脱了"Robeson"上限的限制.     

高分子气体分离膜材料的化学结构与气体透过性能之间的关系

本文以硅橡胶和聚酰亚胺为基础,从高分子的化学组成、分子链段的运动能力、侧基的大小及其作用等几个方面,讨论了聚合物的化学结构对其均质膜的气体选择透过性能的影响,以溶解扩散过程对气体分离膜材料的透气行为进行了剖析,井简述高分子化学结构对其成膜时结晶情况的影响及对气体透过的作用;还概述了气体分离膜科学发展的历史以及基本原理.     

高分子-AlCuCl4膜及其气体透过行为探讨

把对一氧化碳具有选择吸附功能的液体吸附剂(AlCuCl_4-甲苯溶液和AlCuCl_4-Pst-甲苯溶液)引入到高分子(EC、Pst、ABS、CA)膜材料中,制成固体膜,考察了膜的气体透过性能,同时初步得出结果认为,膜中的AlCuCl_4以电荷转移配合物形式与高分子配位结合.     

尼龙6,6膜的电驱动透过性

电驱动条件下膜分离性能的研究对膜在微流控芯片等微小器件中的应用具有重要的指导意义.研究了界面聚合的尼龙6,6膜的电驱动分离性能,并考察了电场强度、通电时间和温度等操作条件对SO42-和Cl-离子透过性能的影响.结果表明尼龙6,6膜具有较好的SO24-和Cl-离子透过性能,并且透过性能差异不大,离子透过百分比随电场强度和通电时间的增加而增加,而随温度的增加基本保持不变.而对FITC标记的甘氨酸和赖氨酸则能完全截留,截留分子量在500左右,具有部分纳滤膜性质.该膜可望应用于微型器件中氨基酸等有机与生物大分子的电驱动分离和浓缩.     

聚三甲硅基丙炔的表面氟化改性及氧氮透过性

对聚三甲硅基丙炔（ＰＴＭＳＰ）进行表面氟化改性，改性膜的氧氮选择性提高，气体透过稳定性增加．用ＸＰＳ谱分析改性后的膜表面，其表面结构发生了显著变化。     

Long-term permeation properties of poly(1-trimethylsilyl-1-propyne) membranes in hydrocarbon—Vapor environment

Poly(1-trimethylsilyl-1-propyne) (PTMSP), a high free-volume glassy di-substituted polyacetylene, has the highest gas permeabilities of all known polymers. The high gas permeabilities in PTMSP result from its very high excess free volume and connectivity of free volume elements. Permeability coefficients of permanent gases in PTMSP decrease dramatically over time due to loss of excess free volume. The effects of aging on gas permeability and selectivity of PTMSP membranes continuously exposed to a 2 mol % n-butane/98 mol % hydrogen mixture over a period of 47 days are reported. The permeation properties of PTMSP membranes are quite stable when the polymer is continuously exposed to a gas mixture containing a highly sorbing organic vapor such af n-butane. The n-butane/hydrogen selectivity was essentially constant for the 47-day test period at a value of 29, or 88% of the initial value of the as-cast film of 33. Condensable gases such as n-butane may serve as a “filler” in the nonequilibrium free volume of the polymer, thereby preserving the high level of excess free volume. © 1997 John Wiley & Sons, Inc. J Polym Sci B: Polym Phys 35 : 1483–1490, 1997     

Transport of organic vapors through poly(1-trimethylsilyl-1-propyne)

Poly(1-trimethylsilyl-1-propyne) [PTMSP], a high-free-volume glassy polymer, has the highest gas permeability of any known synthetic polymer. In contrast to conventional, low-free-volume, glassy polymers, PTMSP is more permeable to large, condensable organic vapors than to permanent gases. The organic-vapor/permanent-gas selectivity of PTMSP based on pure gas measurements is low. In organic-vapor/permanent-gas mixtures, however, the selectivity of PTMSP is much higher because the permeability of the permanent gas is reduced dramatically by the presence of the organic vapor. For example, in n-butane/methane mixtures, as little as 2 mol% n-butane (relative n-butane pressure 0.16) lowers the methane permeability 10-fold from the pure methane permeability. The result is that PTMSP shows a mixed-gas n-butane/methane selectivity of 30. This selectivity is the highest ever observed for this mixture and is completely unexpected for a glassy polymer. In addition, the gas mixture n-butane permeability of PTMSP is considerably higher than that of any known polymer, including polydimethylsiloxane, the most vapor-permeable rubber known. PTMSP also shows high mixed-gas selectivities and vapor permeabilities for the separation of chlorofluorocarbons from nitrogen. The unusual vapor permeation properties of PTMSP result from its very high free volume - more than 20% of the total volume of the material. The free volume elements appear to be connected, forming the equivalent of a finely microporous material. The large amount of condensable organic vapor sorbed into this finely porous structure causes partial blocking of the small free-volume elements, reducing the permeabilities of the noncondensable permanent gases from their pure gas values.     

Polymer characterization and gas permeability of poly(1-trimethylsilyl-1-propyne) [PTMSP], poly(1-phenyl-1-propyne) [PPP], and PTMSP/PPP blends

Pure gas and hydrocarbon vapor transport properties of blends of two glassy, polyacetylene-based polymers, poly(1-trimethylsilyl-1-propyne) [PTMSP] and poly(1-phenyl-1-propyne) [PPP], have been determined. Solid-state CP/MAS NMR proton rotating frame relaxation times were determined in the pure polymers and the blends. NMR studies show that PTMSP and PPP form strongly phase-separated blends. The permeabilities of the pure polymers and each blend were determined with hydrogen, nitrogen, oxygen, carbon dioxide, and n-butane. PTMSP exhibits unusual gas and vapor transport properties which result from its extremely high free volume. PTMSP is more permeable to large organic vapors, such as n-butane, than to small, permanent gases, such as hydrogen. PPP exhibits gas permeation characteristics of conventional low free volume glassy polymers; PPP is more permeable to hydrogen than to n-butane. In PTMSP/PPP blends, both n-butane permeability and n-butane/hydrogen selectivity increase as the PTMSP content of the blends increases. © 1996 John Wiley & Sons, Inc.     

温度对碳膜内氮、氧渗透分离影响的非平衡模拟

采用双控体积巨正则系综分子动力学(DCV-GCMD)方法, 用二维狭缝代替传统的一维狭缝构建膜孔模型研究了温度对氮氧纯气体及其混合物在碳膜内的渗透特性, 探讨了氮氧分离机理. 提出了一种新的计算二元混合气体中各组分通量和分离系数的方法, 即模拟中引入迭代, 解决了前人忽略低压侧气体组成和压力影响的问题. 试验结果表明: 当氮氧以纯气体的形式分别透过碳膜时, 二者均遵循Knudsen扩散方式, 且低温下氮气具有较大的渗透性质; 而当二者以混合物的形式一起透过碳膜时, 低温下二者之间存在竞争吸附, 孔宽对气体的渗透影响显著, 尤其是膜孔较小的时候, 分子筛效应控制氮氧分离; 高温下吸附影响不显著.     

Solution and Diffusion Behavior of Pure Gases and Gas Mixtures in Glassy Polymer Membranes

A general model for the solution and diffusion behavior in pure gas-polymer membrane systems and gas mixture-polymer membrane systems has been developed. Proved by experiments on different glassy and rubbery polymer membranes at various temperatures and pressures, this model can achieve the prediction of permeation behavior of pure gases and gas mixtures in polymer membranes only using the model parameters obtained from experiments on pure gases. The calculated results are in good agreement with experimental.     

混合导体透氧膜及其在甲烷部分氧化制合成气反应中的应用

本文介绍了混合导体透氧膜材料的种类及最新研究进展, 对透氧机理进行了阐述, 对氧透量的理论公式进行了推导, 并对其在甲烷部分氧化制合成气(POM ) 膜反应过程中的应用、材料的要求及膜反应器的构造进行了概述与讨论。     

Surface Modification of Polyimide Membranes by Diamines for H2 and CO2 Separation

Summary: The separation of H₂/CO₂ is technologically important to produce the next generation fuel source, hydrogen, from synthesis gas. However, the separation efficiency achieved by polymeric membranes is usually very low because of both unfavourable diffusivity selectivity and solubility selectivity between H₂ and CO₂. A series of novel diamino‐modified polyimides has been discovered to enhance the separation capability of polyimide membranes especially for H₂ and CO₂ separation. Both pure gas and mixed gas tests have been conducted. The ideal H₂/CO₂ selectivity in pure gas tests is 101, which is far superior to other polymeric membranes and is well above the Robeson's upper‐bound curve. Mixed gas tests show an ideal selectivity of 42 for the propane‐1,3‐diamine‐modified polyimide. The lower selectivity is a result of the sorption competition between H₂ and the highly condensable CO₂ molecules. However, both pure gas and mixed gas data are better than other polymeric membranes and above the Robeson's upper‐bound curve. It is evident that the proposed modification methods can alter the physicochemical structure of polyimide membranes with superior separation performance for H₂ and CO₂ separation.

Both pure gas and mixed gas separation properties of H₂/CO₂ for membranes derived from 6FDA‐durene with respect to the upper‐bound curve.     

碳氟基团修饰的疏水微孔二氧化硅膜制备与表征

采用三氟丙基三乙氧基硅烷（TFPTES）和正硅酸乙酯（TEOS）作为前驱体,通过溶胶-凝胶法制备了三氟丙基修饰的SiO2膜材料。利用扫描电镜、N2 吸附、 红外光谱仪以及视频光学接触角测量仪对膜的断面形貌、孔结构以及疏水性能进行了表征。结果表明,随着三氟丙基三乙氧基硅烷加入量的增大,膜的疏水性逐渐增强,膜的孔结构基本保持不变。当TFPTES/TEOS的摩尔比例达到0.6时,膜对水的接触角达到 111.6°±0.5º,膜材料仍保持良好的微孔结构,其孔体积为0.19cm3•g-1,孔径为0.97nm。     

Thermal Behaviour of PVC/Poly(MMA-co-DVB) Polymer Systems and Membranes Based on PVC/Poly(MMA-co-DVB) Systems

The thermal stabilities of PVC/poly(MMA-co-DVB) polymer systems and membranes prepared by the paste method were investigated. The thermoanalytical curves were used to determine the main thermal stage of the decompositions. It was found that the thermal properties of the polymer systems were affected by the divinylbenzene content. A membrane based on the PVC/poly(MMA-co-DVB) system with 5 mass% DVB displays thermal stability up to 210°C. This revised version was published online in July 2006 with corrections to the Cover Date.