聚1—三甲硅基丙炔膜的溴化和气体透过性

在新的气体分离膜材料中,聚1-三甲硅基丙炔(PTMSP)以其高的气体透过性和优异的成超薄膜性而引起各方面的兴趣。目前的研究热点是如何提高PTMSP的氧氮透过分离系数(ao_2/N_2)和气体透过稳定性。Langsam用氮稀释的氟气对PTMSP膜进行表面氟化处理,大幅度地提高了膜的ao_2/N_2,但处理过程中伴随着剧烈的裂解,控制困难。Gozds以N-溴代丁     

D_4等离子体聚合物复合膜的制备、形成过程及其氧氮分离性

<正> 将高分子膜用于气体分离已越来越受到人们的重视.在特定条件下,用等离子体聚合可形成高分子超薄膜,它有高度交联结构,表面平整、致密、无针孔.因此,将它用于气体分离是有希望的.本工作用八甲基环四硅氧烷(简称D_4)作单体,进行等离子体聚合,沉积在聚丙烯多孔底膜上,得到D_4等离子体聚合物复合膜.研究表明,该膜有较好的气体透过性能,其氧气透过速率Jo_2为0.5—2×10~(-5)cm~3(STP)/cm~2·sec·cmHg,氧氮分离系数。αo/N为3.3—3.8,远远高于用经典方法制得的聚有机硅氧烷膜的αo/N2.0.     

新型含钴硅橡胶离聚体膜的富氧性能

硅橡胶 ( PDMS)是最早使用的气体分离膜材料 ,其氧透过系数较高 ( PO2 =6 0 0 Barrer) ,但氧氮分离系数低 ( αO2 /N2 =2 .0 ) ,成膜性及膜强度差 ,因而限制了其应用 .PDMS改性一直是气体分离膜研究的重要课题[1] ,提高氧氮分离性 ,改善成膜性 ,而不影响其透气性 ,成为人们追求     

等离子体改性提高PTMSP膜氧氮选择性

膜材料中迄今以聚三甲基硅基丙炔(PTMSP)的透气速率最大,其氧透过速率比PDMS高一个数量级,但氧氮分离系数小,透气性不稳定。改性PTMSP,以提高其透气选择性和透气速率稳定性引起人们的极大关注。本文报道,在外极管式电容耦合反应器中,     

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.     

溴代聚-4-甲基戊烯-1的溶解性能及其膜的形态结构和结晶状态

<正> 迄今为止,用于气体分离的高分子膜,其气体透过速率和选择分离系数仍不够高。究其原因,一是膜材料的气体透过系数较低;二是某些气体透过系数较高的高分子材料又难以形成超薄膜层。     

TMSP—PMDSP共聚物膜的氧,氮透过性

研究了三甲基硅丙炔(TMSP) 和五甲基二硅丙炔(PMDSP) 的共聚物膜对O_2、N_2气体的透过行为。发现 TMSP-PMDSP共聚物膜对O_2、N_2气体的透过活化能为负值,透过系数随温度升高而下降;受热历程不同,气体在膜中的透过行为也不相同。膜两侧气体压差不同时,气体在膜中的透过系数亦发生变化。用氟化物HFBM对共聚物膜表面进行了化学改性,改性膜的P_(O_2)/PN_2值达到3.52。     

体积法测量聚合物膜透气速率方法的改进

最近几年,我国利用合成高分子膜选择性分离各种气体的工作,取得了快速的进展。例如氮-氢分离膜,富氧膜等,都有一些单位在进行深入的研究。当需要测量聚合物膜的透气速率时,一般均采用国外标准办法。常用的有ISO2556(1974),BS2782Part8(1979)821A,DIN53380(1969)或ASTMD1434(1975)。其中美国ASTM1434“塑料薄膜和薄片气体透过速率的标准测试方法”,包括压力法和体积法。本文仅讨论对体积法的改进。该法所用的测试仪器为CSI-135型,美国Custom Scientific Instrument In.Co.公司的产品。图1为该仪器的示意图。     

过渡金属有机络合物添加剂对聚酰亚胺气体分离膜性能的影响

采用具有庞大取代基团的过渡金属有机络合物作为添加剂制备了聚酰亚胺气体分离膜,研究了过渡金属盐、有机配体和金属络合物对聚酰亚胺均质膜和非对称膜氢、氮气体透过性能的影响,结果表明过渡金属盐添加剂提高了分离系数,但降低了气体透过速率;有机配体添加剂增大了气体透过速率却降低了分离系数;以络合物作添加剂时,可在不降低分离系数的情况下使气体透过速率得到提高,是一种改进气体分离膜性能的有效方法。     

溴代及胺交联聚苯醚（PPO）膜的气体透过行为

对聚苯醚(PPO)进行了苯环溴代、甲基溴代以及胺交联,发现苯环溴代可提高O_2、N_2透过率(P),而选择性(α)基本不变。甲基溴代则相反,P降低、α有明显提高。调节两者比例可得到P、α兼优的O_2、N_2分离膜。甲基溴代后进一步胺交联可得到α更高、耐溶剂的膜材料。     

Gas transport properties of thin polymeric membranes in the presence of silicon dioxide particles

The fundamental gas transport properties of thin films of six high performance polymers were evaluated in the presence of silicon dioxide particles. The silica particles were brought in close contact with the polymer inside the 200 Å. (DIA) pores of Anopore™ aluminum oxide membranes. This unique environment allows intimate contact between the polymer and the silica particles. The presence of silica improves the gas separation properties of the permselective layer, particularly for oxygen and nitrogen. The increase in O₂/N₂ selectivity for some membranes is accompanied by an increase in oxygen permeability. The oxygen/nitrogen separation properties of the polymers in the presence of silica falls above the so-called “upper limit” of performance reported for polymeric materials. The observed significant increases in the glass transition temperature suggest restriction of chain segmental mobility possibly due to adsorption of polymer to silica surface. The increase in the activation energy of permeation points to increases in energetics of diffusion as the reason for the improved selective permeation. The observed behavior was not limited to oxygen and nitrogen as demonstrated by the results for other gas pairs tested.     

成膜溶剂对聚4-甲基戊烯-1膜的形态结构和透过行为的影响——Ⅱ.膜的气体透过行为

以聚4－甲基戊烯－1（PMP）为膜材质，分别以环己烷、三氯乙烯、四氯乙烯及环己烷／三氯乙烯为溶剂，研究了这些溶液浇铸膜对O2、N2、H2及CO2等气体的透过行为。结果表明，气体的透过主要发生在PMP的无定形区域，但也在PMP的晶区进行。PMP的Ⅵ型结晶比Ⅰ型结晶具有较低的氧化透过活化能。     

成膜溶剂对聚4-甲基戊烯-1膜的形态结构和透过行为的影响——Ⅱ.膜的气体透过行为

以聚4-甲基戊烯-1(PMP)为膜材质,分别以环己烷、三氯乙烯、四氯乙烯及环已烷/三氯乙烯为溶剂,研究了这些溶液浇铸膜对O_2、N_2、H_2及CO_2等气体的透过行为。结果表明,气体的透过主要发生在PMP的无定形区域,但也在PMP的晶区进行。PMP的Ⅵ型结晶比Ⅰ型结晶具有较低的气体透过活化能。     

Separation and permeation characteristics of a DD3R zeolite membrane

Permeation of various gases (carbon dioxide, nitrous oxide, methane, nitrogen, oxygen, argon, krypton, neon) and their equimolar mixtures through DD3R membranes have been investigated over a temperature range of 220–373 K and a feed pressure of 101–400 kPa. Helium was used as sweep gas at atmospheric pressure. Adsorption isotherms were determined in the temperature range 195–298 K, and modelled by a single and dual site Langmuir model. The permeation flux is determined by the size of the molecule relative to the window opening of DD3R, and its adsorption behaviour. As a function of temperature, bulky molecules (methane) show activated permeation, weakly adsorbing molecules decreasing permeation behaviour and strongly adsorbing molecules pass through a maximum. Counter diffusion of the sweep gas (helium) ranged from almost zero up to the order of the feed gas permeation and was strongly influenced by the adsorption of the feed gas.

DD3R membranes have excellent separation performance for carbon dioxide/methane mixtures (selectivity 100–3000), exhibit good selectivity for nitrogen/methane (20–45), carbon dioxide and nitrous oxide/air (20–400), and air/krypton (5–10) and only a modest selectivity for oxygen/nitrogen (2) separation. The selectivity of mixtures of a strongly and a weakly adsorbing component decreased with increasing temperature and pressure. The selectivity of mixtures of weakly adsorbing components was independent of pressure.

The permeation and separation characteristics of light gases through DD3R membranes can be explained by taking into account: (1) steric effects introduced by the window opening of DD3R leading to molecular sieving and activated transport, (2) competitive adsorption effects, as observed for mixtures involving strongly adsorbing gases, and (3) interaction between diffusing molecules in the cages of the zeolite.     

Epoxidation of styrene–butadiene–styrene block copolymer and use for gas permeation

The epoxidation of styrene–butadiene–styrene triblock copolymer (SBS) by an in situ generated peracid method is discussed. The presence of an acid acting as catalyst led to side reaction. The reactivities of internal double bonds (the 1, 4-structure) were higher than those of the vinyl bonds (the 1, 2-structure). In the 1, 4-structure, the reactivities of cis-structure were higher than those of trans-structure. The oxirane weight content and total oxygen weight content were determined by titration and element analysis, respectively. The cohesive energy, solubility parameter, and the glass transition temperature of epoxidized SBS increased with increasing total oxygen weight content. But the molecular weight between crosslinking points decreased resulting in an increase of crosslinking density with increasing total oxygen weight content. The changes of properties of epoxidized SBS reduced the gas permeability of oxygen and nitrogen through epoxidized SBS membrane, but increased the gas selectivity between oxygen and nitrogen. When the operating temperature of gas permeation was increased, the permeability of oxygen and nitrogen increased but the selectivity decreased. For epoxidized SBS containing 7.35 wt % oxygen content, the activation energy was 9 and 12.2 kcal/mol for oxygen and nitrogen, respectively.     

Gas transport in vulcanized natural rubber‐cellulose. II. Composites

This work reports the transport of carbon dioxide, oxygen, and nitrogen in amorphous membranes of vulcanized natural rubber reinforced with regenerated cellulose. The values of the permeability coefficient of carbon dioxide, oxygen, and nitrogen in the composites with 25% of cellulose, measured at 25 °C and 15 cmHg of pressure, are roughly one‐third of those measured in the same conditions for these gases in natural rubber. The isotherms representing the variation of both the permeability and diffusion coefficients of the gases with pressure present a relatively sharp increase in the region of low pressures, attributed to changes in the free volume. The analysis of the permeability characteristics of the membranes in terms of the free‐volume theory suggests that gas transport is severely hindered in both the cellulose phase and the cellulose–rubber interphase of the composites. © 2000 John Wiley & Sons, Inc. J Polym Sci B: Polym Phys 38: 393–402, 2000     

Systematic investigation of the effects of temperature and pressure on gas transport through polyurethane/poly(methylmethacrylate) phase-separated blends

Polyurethane (PU) and polyurethane–poly(methylmethacrylate) (PMMA) blend membranes were used in gas separation studies. The effects of blend composition, temperature, and pressure on the permeability, diffusivity, and solubility of CO₂, H₂, O₂, CH₄, and N₂ were investigated. The separation factors of some gas pairs were also evaluated. Positron annihilation lifetime spectroscopy was applied to assess free volume changes as a function of blend composition and temperature. Free volume size increases by approximately 30% with increasing temperature from 10 to 40 °C for all blends studied. The permeability of all gases decreases by approximately 55% with the addition of 30 wt% of PMMA. The permeation process is governed by diffusion, except that of CO₂. In relation to the behavior of gas transport as a function of temperature, some important observations are (i) CO₂ presents the lowest permeation activation energy value (28 kJ/mol), and (ii) gas pair selectivity increases at low temperatures and is high for gas pairs that present differences in permeation activation energies as high as 15 kJ/mol for the CO₂/CH₄ gas pair. Furthermore, the study with pressure variations shows that: (i) at elevated pressure, the PU and the blend membrane permeability to CO₂ and H₂ increases by approximately 35%, and (ii) oxygen-to-nitrogen selectivity increases with pressure as a consequence of the decrease in the permeability to nitrogen in the case of the 30%-PMMA blend.     

Effect of carrier concentration on the facilitated oxygen transport in a polymer membrane

Facilitated transport of oxygen in a solid Polymer membrane containing cobaltporphyrin (CoP) which carries oxygen specifically and reversibly, leads to permselectivity of oxygen against nitrogen in the membrane. The increase in concentration of the CoP carrier is expected to enhance the oxygen transport. The membranes of poly(octylmethacrylate-co-vinylimidazole) containing 0.8 ～ 10 wt% CoP were prepared, and the effects of the CoP-concentration on the transport and the diffusion constants of oxygen are studied. Although the induction period before the steady state of oxygen permeation was prolonged with the CoP concentration in the polymer membrane, the glass transition temperature (T_g) of the membrane was increased and the diffusion constants of oxygen were decreased with the CoP concentration to yield unexpected reduction of the oxygen permeation in the highly CoP loaded membrane.