硅树脂/硅橡胶杂化膜的制备及性能研究

以十三氟辛基三乙氧基硅烷、四甲基二乙烯硅氧烷、乙烯基三甲氧基硅烷和正硅酸乙酯为原料,通过水解缩合制备了乙烯基含氟硅树脂。乙烯基硅橡胶和乙烯基含氟硅树脂为基质材料,含氢硅油为交联剂,硅氢加成制备了改性硅橡胶杂化膜材料。透气性能测试表明,当含氟硅树脂质量分数50.0%时,膜的成膜性和富氧性能之间达到最佳平衡点,30℃和0.01 MPa压差下,P（O2）为628 Barre,a（O2/N2）为3.36。与普通乙烯基硅橡胶交联膜比,这种有机―无机杂化膜在保持原有氧气透过系数的基础上,较好的改进了氧氮分离性能。     

负载钴离子含氟硅橡胶杂化膜的制备及富氧性能

以乙丙橡胶来负载钴离子,并与含氟硅树脂一起引入到硅橡胶中,通过硅氢加成反应,在室温下制备出一种新型三元杂化膜。试验结果表明,在30℃和0.025 MPa压差条件下,三元杂化交联膜的P(O_2)和a(O_2/N_2)分别为684 Barrer和7.49,分离性能明显优于普通的含氟硅橡胶膜,富氧性能也超越了Robeson上限。与普通的含氟硅橡胶膜相比,钴离子络合物可与含氟组分之间可产生协同作用,使得对氧的促进输送作用更为显著,从而导致其氧氮分离性能进一步提高。乙丙橡胶具有良好的韧性可改善硅树脂引入而产生的变脆。     

改性硅橡胶富氧膜的制备

富氧膜是近年来发展起来的一种能制备富氧空气的新技术。目前国内外使用最广的富氧膜材料是甲基硅氧烷(通常称为硅橡胶)它的透氧系数Po_2=6×10~(-8)cm~3(STP)·cm/cm~2·S·cmHg,C_(O_2/N_2)=2.0,透气速度快,但机械性能较差,须予以改性,改     

聚砜基膜成膜条件与富氧膜性能之间的关系

以聚砜为基膜材料,采用正交实验方法制备了平板超滤膜,然后在其表面涂敷改性聚二甲基硅氧烷后制得聚砜-硅橡胶复合型富氧膜,并研究了复合富氧膜性能与基膜成膜条件之间的关系。研究结果表明:当聚砜含量为20.15%,N-甲基吡咯烷酮含量为70.37%,聚乙二醇-600含量为9.48%时,制得的复合富氧膜的富氧浓度可达28.8%,渗透系数为7.02×10-4m3/(m2.S.MPa)。此外,还用扫描电镜观察复合富氧膜的基膜的结构特点。     

有机-无机杂化分离膜研究进展

有机-无机杂化膜材料结合了有机膜材料和无机膜材料的优良性能,已成为分离膜材料研究的一个热点。本文以有机、无机组分间相互作用类型对其进行分类,着重介绍组分间以化学键相结合的有机-无机杂化膜的优良特性,总结了影响此类杂化膜结构和性能的主要因素,概括了它在膜分离中的应用,提出了目前研究工作中存在的不足,并做出了简要的述评。     

乙基纤维素三甲硅基衍生物膜的结构表征与氧氮渗透行为

气体分离膜是近年发展起来的应用前途广阔的一个领域。近年来由于非对称膜技术的开发,美国和日本已开始用硅橡胶涂复在多孔聚砜上制成PDMS-PS复合膜。PDMS是透气量最高而稳定的膜材料,但氧氮分离系数仅为2。 乙基纤维素(EC)具有机械强度高、抗热、耐寒和稳定性好等优点,是一种具有潜力的优秀膜材料。其中取代基的位置和含量对膜的性能有较大的影响。日、美等国科学家利用EC对氧氮的良好分离系数制成了中孔纤维材料富氧器、EC涂复在聚二甲基硅氧     

聚酰亚胺-二氧化硅杂化膜的制备及表征

 采用溶胶－凝胶法制备了两类具有不同二氧化硅含量的聚酰亚胺－二氧化硅（PI－SiO2）杂化膜,并用SEM,IR,TG－DTA,氮吸附和气体渗透性能测试等手段对该膜材料的表面形貌、结构、热性能、孔径分布和气体渗透性能进行了表征．结果表明,PI－SiO2膜材料中SiO2粒子的分散良好,与有机相之间存在着分相和键联;膜材料的玻璃化温度θg均随SiO2含量的增加而升高．相比之下,在酸性条件下制备的T系列杂化膜比在碱性条件下合成的S系列杂化膜对θg的影响更大一些;杂化膜具有较好的气体渗透性能和亲水性能,其H2O／N2和H2O／CH4的分离系数远大于努森扩散的理论值．     

F127反相微乳液的组成对AgCl纳米粒子形成及AgCl/F127-PMMA杂化膜结构和性能的影响

以F127为表面活性剂构成的反相微乳液制备AgCl纳米粒子和AgCl/F127-PMMA杂化膜,通过紫外可见光谱(UV-visible)、透射电镜(TEM)研究了微乳液的增容水量(ω)和盐浓度(Csalt)对AgCl粒子形成与形貌的影响;结合表面ζ电位测定、扫描电镜(SEM)分析和溶胀实验等考察了AgCl/F127-PMMA杂化膜的结构和性能。研究结果表明,低ω下盐浓度增加,胶束中AgCl反应速率增大,导致大量小粒径AgCl粒子的形成;高ω下盐浓度增加,将加快AgCl粒子的生长,从而导致胶束中的AgCl粒子粒径增大;各种ω下盐浓度的增加,都会引起胶束中单质Ag的形成。杂化膜的SEM分析显示,AgCl粒子粒径越小,在杂化膜中的分散性越好,膜表面的ζ电位也越高,膜在苯中的溶胀性能也越高;单质Ag的出现和AgCl粒子数目的增多,杂化膜中将显现明显的粒子团聚现象,这极大地影响了杂化膜在苯中的溶胀性能;而杂化膜在环己烷中的溶胀性能较低,且随ω和盐浓度的变化极小。     

LTV—PSF富氧膜的复合机理研究

用不同种类和浓度的极性有机物水溶液(醇-水溶液、羧酸-水溶液、多官能团有机物-水溶液)以及四种类型(阳离子、阴离子、两性、非离子)表面活性剂水溶液处理聚砜支撑膜改变其表面化学特性,改善硅橡胶汽油溶液在其表面的铺展性能;用两次浸泡减少涂层过程中硅橡胶汽油溶液向支撑膜内的渗透程度,使LTV-PSF复合膜的透量获得较大幅度的提高。同时考察了聚砜支撑膜结构因素的影响。     

多金属氧簇与倍半硅氧烷簇构筑的哑铃形杂化分子Langmuir膜和Langmuir-Blodgett膜

以两个形状杂化分子(Shape Hybrid Molecules)为目标分子, 研究了它们在气液界面上形成Langmuir膜的过程和Langmuir-Blodgett (LB)膜的聚集态结构. 杂化分子是由Wells-Dawson型磷钨氧簇(Polyoxometalates, POMs)和T₈型的倍半硅氧烷簇(Polyhedral Oligosilsesquioxane, POSS), 通过对苯二甲酸有机连接链(OL)用共价键构筑的具有杂化性质和哑铃形状的簇-簇杂化分子(POM-OL-POSS). 这两种杂化分子的差别在于POSS段中, 外围有机基团的尺寸不同. 在实验中, 采用Langmuir和LB膜技术, 了解POSS外围的七个取代基变化导致的分子尺寸变化对Langmuir膜形成过程和LB膜结构的影响. 采用Langmuir技术测定了表面压-平均分子面积(π-A)等温曲线和π-A循环等温曲线, 跟踪并研究了这两个杂化分子在水表面上形成Langmuir膜的过程. 实验结果表明, 两个杂化分子都表现出良好的两亲性, 从气相变化到固相的过程中, 杂化分子经历了从分散到集中的过程. 将这些膜转移到基片上, 得到单层的LB膜, 再利用原子力显微镜(AFM)和透射电子显微镜(TEM)研究了LB膜的表面形貌和聚集态结构. 由于POM段中含有钨和钒金属, 可以直接用TEM观察聚集态结构, 发现了在气-液和液-固相转变过程中, LB膜中杂化分子的聚集态结构都呈现涨落特征, 一种凝聚态物理中由相转变导致结构涨落的重要物理现象. 本研究获得的结果能够帮助我们以及这个领域的研究者们继续优化杂化分子的结构, 进一步构筑具有有序结构的膜和本体材料.     

荷电膜的膜电位研究进展

膜电位的测定是表征荷电膜的传递现象的重要参数之一。本文简要介绍了膜电位理论基础,包括T. M. S.理论和不可逆热力学理论。分别阐述了关于离子交换膜、双极膜、两性膜以及复合膜的膜电位的最新进展,并提出今后的发展方向。     

透氢钯复合膜的原理、制备及表征

钯及其合金膜由于具有透氢性好和耐高温的特点,除了用作氢气分离和纯化器外,还可以用作脱氢、制氢等反应的反应器,以实现反应和分离的一体化,并提高转化率和选择性。本文综述了钯基复合膜的原理、制备及表征,并重点介绍了本研究组的光催化镀膜工艺。     

高分子纳滤膜的研究及进展

对高分子纳滤膜的发展背景以及国内外在这一领域的研究的研究进展作了详细的介绍。     

透氢钯复合膜的原理、制备及表征

钯及其合金膜由于具有透氢性好和耐高温的特点,除了用作氢气分离和纯化器外,还可以用作脱氢、制氢等反应的反应器,以实现反应和分离的一体化,并提高转化率和选择性。本文综述了钯基复合膜的原理、制备及表征,并重点介绍了本研究组的光催化镀膜工艺。     

纳米复合膜在膜分离领域的研究进展

基于纳米材料的独特性质,将其引入高分子膜所制得的纳米复合滤膜有望解决目前制约膜技术发展的“上限平衡”问题。 本文综述了碳纳米管、石墨烯、SiO2、TiO2、分子筛、ZrO2以及纳米银颗粒等纳米复合膜在膜分离领域的研究进展。 这些纳米材料对于提高复合膜的机械稳定性、亲水性、选择性、渗透性及抗污染能力等有显著的效果。 此外,对纳米复合膜的发展与应用做了展望,也对其研究中存在的问题和解决方法进行了阐述。     

Preparation of Zeolite X Membranes on Porous Ceramic Substrates with Zeolite Seeds

Zeolite X membranes were investigated by in-situ hydrothermal synthesis on porous ceramic tubes precoated with zeolite X seeds or precursor amorphous aluminosilicate, and porous α-Al2O3 ceramic tubes with a pore size of 50 200 nm were employed as supports. Zeolite X crystals were synthesized by the classic method and mixed into deionized water as a slurry with a concentration of 0.2 0.5wt%, having a range of crystal sizes from 0.2 to 2μm. Crystal seeds were pressed into the pores near the inner surface of the ceramic tubes, and crystallization took place at 95℃ for 24-96 h. It was also investigated that Boehmite sol added with zeolite X seeds was precoated on ceramic supports to form a layer of γ-Al2O3 by heating, and hydrothermal crystallization could then take place to prepare the zeolite membranes on the composite ceramic tubes. The crystal species were characterized by XRD, and the morphology of the supports subjected to crystallization was characterized by SEM. The composite zeolite membranes have zeolitic top-layers with a thickness of 10-25 μm, and zeolite crystals can be intruded into pores of the supports as deeply as 100μm. The experimental results indicate that the precoating of zeolitic seeds on supports is beneficial to crystallization by shortening the synthesis time and improving the membrane strength. The resulting zeolite X membrane shows permselectivity to tri-n-butylamine((C4H9)3N) over perfluro-tributyl-amine ((C4Fg)3N), and a permeance ratio of 57 for ((C4Hg)3N to (C4F9)3N could be reached at 350℃. Permeances of BZ, EB and TIPB through the zeolite membrane were also measured and were found to slightly increase with temperature.     

氯化锂为添加剂制得的疏水聚偏氟乙烯不对称微孔膜的形态结构及其膜蒸馏性能

结合膜的形态结构研究了以 LiCl为添加剂制得的疏水 PVDF膜的膜蒸馏性能。与来用水溶液高分子添加剂制得的PVDF微孔膜相比,膜蒸馏性能有了较大提高,尤其具有更高的截留率。制得的微孔膜的蒸馏通量已接近商品膜的膜蒸馏通量,表明以LiCl为添加剂制得的PVDF疏水微孔膜是一种适用于膜蒸馏的较理想的疏水微孔膜。     

PREPARATION OF SILICALITE-1 AND ZSM-5 ZEOLITE/ CERAMIC COMPOSITE MEMBRANES

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Preparation of Zeolite X Membranes on Porous Ceramic Substrates with Zeolite Seeds

Zeolite X membranes were investigated by in-situ hydrothermal synthesis on porous ceramic tubes precoated with zeolite X seeds or precursor amorphous aluminosilicate, and porous α-Al2O3 ceramic tubes with a pore size of 50-200 nm were employed as supports. Zeolite X crystals were synthesized by the classic method and mixed into deionized water as a slurry with a concentration of 0.2-0.5wt%, having a range of crystal sizes from 0.2 to 2μm. Crystal seeds were pressed into the pores near the inner surface of the ceramic tubes, and crystallization took place at 95℃ for 24-96 h. It was also investigated that Boehmite sol added with zeolite X seeds was precoated on ceramic supports to form a layer of r-Al2O3 by heating, and hydrothermal crystallization could then take place to prepare the zeolite membranes on the composite ceramic tubes. The crystal species were characterized by XRD, and the morphology of the supports subjected to crystallization was characterized by SEM. The composite zeolite membranes hav     

Theoretical analysis of the performance of composite membrane consisting of the catalytic and nanofiltration layers

A model of the composite membrane consisting of the catalytic layer (CL) and the nanofiltration layer (NFL) is presented. It has been found that applying NFL on the permeate side of CL it is possible to enhance substantially the conversion of substrate into the product. The best performance is obtained for high retention of substrate and low of product. At higher values of volume flow and/or longer catalytic path the retention degree of product becomes negligible. The presence of NFL enhances the influence of distribution of the reaction rate constant, k, on the conversion ratio. Comparing to k = constant the positive effect is obtained if k increases along the catalytic pore, whereas negative—if k decreases.