高硅ZSM—5沸石填充硅橡胶膜的研究（Ⅳ）：沸石粒径和不同品…

研究了粒径为１５μｍ和５μｍ的水热处理Ｓｉｌｉｃａｌｉｔｅ－Ｉ填充ＰＤＭＳ膜以及酸处理Ｓｉｌｉｃａｌｉｔｅ－Ｉ填充不同品种硅像胶膜对低浓度乙醇－水混合物的渗透发分离性能的影响。结果表明，沸石粒径的减小，不利于乙醇－水分离系数的提高；不同品种硅橡胶有沸石充膜对乙醇－水的渗透蒸发分离性能与硅橡胶本身的性质有关。     

酸处理Silicalite—Ⅰ沸石填充硅橡胶渗透蒸发分离膜

研究酸处理Ｓｌｉｌｉｃａｌｉｔｅ－Ⅰ沸石对有机溶剂、水的吸附、脱附性质，酸处理Ｓｉｌｉｃａｌｉｔｅ－Ⅰ填充硅橡胶对低浓度有机溶剂水溶液的渗透蒸发分离性能以及填充膜的力学性能。实验结果表明，在硅橡胶胶膜中填充酸处理Ｓｉｌｉｃａｌｉｔｅ－Ⅰ沸石能改善膜对有机溶剂－水混合物的分离性能，且分离性能的改善与沸石在膜中的填充量以及硅橡胶的品种有关。另外，沸石的填充也有利于改善膜的力学性能。     

酸处理Silicalite—I沸石填充硅橡胶渗透蒸发分离膜

研究酸处理Ｓｉｌｉｃａｌｉｔｅ—Ｉ沸石对有机溶剂、水的吸附、脱附性质，酸处理Ｓｉｌｉｃａｌｉｔｅ—Ｉ填充硅橡胶膜对低浓度有机溶剂水溶液的渗透蒸发分离性能以及填充膜的力学性能。实验结果表明，在硅橡胶膜中填充酸处理Ｓｉｌｉｃａｌｉｔｅ—Ｉ沸石能改善膜对有机溶剂－水混合物的分离性能，且分离性能的改善与沸石在膜中的填充量以及硅橡胶的品种有关。另外，沸石的填充也有利于改善膜的力学性能。     

填充沸石的聚乙烯醇膜的性质及其在催化酯化反应中的应用

考察了KA、NaA、CaA及NaX沸石填充的聚乙烯醇膜在不同醇/水体系中的分离性能,发现经沸石填充后膜的通量增加,而分离系数的升降则取决于被分离醇分子及沸石的孔径大小。对于小分子醇/水体系,填充膜分离系数下降,反之则上升。经考察KA填充膜对乙酸乙酯化和水杨酸甲酯化的膜助催化反应发现,填充膜对反应的推动作用较未改性膜有了进一步的提高。     

高硅ZSM－5沸石填充硅橡胶膜的研究（Ⅳ）──沸石粒径和不同品种硅橡胶对乙醇－水混合物渗透蒸发分离性质的影响

研究了粒径为１５μｍ和５μｍ的水热处理Ｓｉｌｉｃａｌｉｔｅ－Ⅰ填充ＰＤＭＳ膜以及酸处理Ｓｉｌｉｃａｌｉｔｅ－Ⅰ填充不同品种硅橡胶膜对低浓度乙醇－水混合物的渗透蒸发分离性能的影响。结果表明，沸石粒径的减小，不利于乙醇－水分离系数的提高；不同品种硅橡胶的沸石填充膜对乙醇－水的渗透蒸发分离性能与硅橡胶本身的性质有关。     

高硅ZSM—5沸石填充硅像胶膜的研究（Ⅲ）：对纯溶剂的吸附…

研究Ｓｉｌｉｃａｌｉｔｅ－Ｉ填充ＰＤＭＳ膜对乙醇和水的吸附、脱附和渗透蒸发性质以及吸附膜中丙酮在ＤＳＣ测试中的行为。结果表明，沸石填充膜对乙醇的吸附量和渗透蒸发通量均明显高于水，且乙醇的沸石填充膜中达到吸附、脱附平衡的速度均快于水；且吸附在填充和不填充沸石的硅橡胶膜中丙酮的熔融温度有明显的提高，说明硅橡胶膜与有机溶剂有较强的相互作用。此外，沸石填充膜的结构在３０ｗｔ％填充量附近有一改变，表明膜中硅     

水热处理Silicalite—Ⅰ沸石填充硅橡胶膜Ⅰ对有机溶剂──水混合物的渗透蒸发分离性质

研究水热处理Ｓｉｌｉｃａｌｉｔｅ—Ⅰ沸石对乙醇和水的吸附、脱附性质以及其填充ＰＤＭＳ膜对乙醇、水的渗透蒸发通量和对低浓度有机溶剂一水混合物的渗透蒸发分离性能。实验结果表明，Ｓｉｌｉｃａｌｉｔｅ—Ⅰ沸石经水热处理，其水吸附量大为减少，因此其填充ＰＤＭＳ膜对有机溶剂－水混合物，主要是醇－水混合物的分离系数有显著提高。     

多孔壳聚糖膜对醇—水体系中醛的吸附性能

研究了多孔壳聚糖膜对乙醇－水混合体系中微量醛的吸附性能。通过对影响其吸咐性能的各种因素如壳聚糖膜的制备方法。用量、醇－水体中醇浓度、酸度及其温度等的研究,认为壳聚糖适用于醇－水混合体系中微量醛的清除,并据此提出了吸附操作的优化条件。     

高硅ZSM-5沸石填充硅橡胶膜的研究(Ⅱ)——渗透蒸发性质的影响因素

研究了沸石的处理方式、渗透蒸发体系的组成以及醇-水混合物中氢键的变化对Silicalite-I沸石填充聚二甲基硅橡胶膜渗透蒸发性质的影响.实验结果表明,沸石经水热处理以及在醇-水混合物中加入盐、酸等电解质能提高膜对醇-水混合物的分离性能.     

填充Silicalite—I沸石的PDMS橡胶醇—水分离膜

Ｓｉｌｉｃａｌｉｔｅ－Ｉ沸石经过酸处理或水热处理可完善其晶体结构，提高对乙醇的吸附选择性，由此提高对乙醇－水混合物的分离系数，特别是先经过酸处理再经过水解处理的Ｓｉｌｉｃａｌｉｔｅ－Ⅱ沸石填充聚二甲基硅氧烷橡胶膜，乙醇－水的分离系数可达３０左右。     

Copper-exchanged LTA zeolite membranes with enhanced water flux for ethanol dehydration

Phase-pure and well-intergrown Cu-LTA membranes are developed through copper ions exchange of sodium ions in Na-LTA framework. For pervaporation of 90.0 wt% ethanol/10.0 wt% water mixtures, the Cu-LTA membrane shows much higher water flux than Na-LTA membranes due to the enhancement of the pore size after ions exchange.     

ZSM-5分子筛填充壳聚糖膜的制备与性能研究

采用液相共混的方法制备了ZSM-5分子筛填充壳聚糖膜.扫描电镜表征表明分子筛在膜中分散均匀,膜表面没有明显缺陷.考察了填充膜在碳酸二甲酯/甲醇混合液中的溶胀和吸附行为,探讨了填充膜中分子筛含量及操作温度对渗透汽化膜分离性能的影响.结果表明膜优先吸附甲醇,其分离性能主要由溶解过程控制;随着膜中分子筛含量的增加,膜的溶胀度增大,渗透通量大幅度提高;渗透通量与操作温度符合Arrhenius关系式.与壳聚糖均质膜相比,ZSM-5分子筛填充壳聚糖膜对甲醇和碳酸二甲酯混合物具有更好的分离效果.     

Water-alcohol Separation by Pervaporation through Zeolite Modified Poly(amidesulfonamide)s (PASAs)

A series of poly(amidesulfonamide)s (PASAs) which have been synthesized in our laboratory possess good membrane fabrication properties^[1]. The potential use of these membrane materials in RO, UF and PV were demonstrated^[2,3]. Reminiscent to the PV performance of other glassy polymers, most of these materials exhibit a fairly high separation factor albeit a permeation flux below 35 g m^-2 h^-1 in the PV separation of aqueous alcohol mixtures. To have a real application prospect in PV, the permeation flux through the membranes has to e further improved. The present work represents our effort to upgrade the separation characteristics of PASAs by blending with inert hydrophilic zeolites. Three types of PASAs (structure shown in Figure 1) were selected to be fabricated by blending different amount of zeolite NaA or NaX. The zeolite filled membranes were characterized by SEM, IR spectroscopy, sorption measurements and wide-angle X-ray diffraction. By adding proper amount of NaA into the polymer casting solutions, the resultant zeolite filled membranes exhibited improvement in both selectivity and permeability in the separation of 10% aqueous solutions of ethanol, propan-l-ol and propan-2-ol, as compared to the zeolite free membrane (Table 1).     

PERVAPORATION OF ETHANOL/WATER MIXTURES WITH HIGH FLUX BY ZEOLITE-FILLED PDMS/PVDF COMPOSITE MEMBRANES

Thin-film zeolite-filled silicone/PVDF composite membranes were fabricated by incorporating zeolite particles into PDMS(poly(dimethylsiloxane)) membranes.The morphology of zeolite particles and zeolite filled silicone composite membranes were characterized by SEM.The zeolite-filled PDMS/PVDF composite membranes were applied for the pervaporation of ethanol/water mixtures and showed higher flux compared with that reported in literatures.The effect of zeolite loading and Si/Al ratio of zeolite particles on...     

二次生长法制备高分离性能的PHI分子筛膜

通过二次生长法在α-Al2O3支撑体表面合成了PHI分子筛膜,考察了晶种合成方式、二次生长合成温度及时间对形成PHI分子筛膜的影响.采用X射线衍射(XRD)、扫描电子显微镜(SEM)对合成膜进行表征.结果表明:载体表面合成出了PHI分子筛;二次生长法合成出的PHI分子筛膜连续、致密,膜厚约为20 μm.利用渗透汽化技术对甲醇、乙醇、异丙醇和叔丁醇等不同分子尺寸的醇/水体系进行分离性能的研究,同时考察原料液中水含量对所制备的PHI分子筛膜的分离性能的影响.结果表明:PHI分子筛膜对几种醇水体系都具有良好的分离效果,随着水含量的增加,水的渗透通量呈增大趋势,乙醇和甲醇的理想分离因子有所降低,异丙醇和叔丁醇的理想分离因子增大.     

Pervaporation separation of ethanol/water mixtures with chlorosilane modified silicalite-1/PDMS hybrid membranes

<正>Ultra-fine silicalite-1 particles were modified with four kinds of chlorosilanes(dodecyltrichlorosilane, octyltrichlorosilane,hexadecyltrichlorosilane and octadecyltrichlorosilane) and characterized by FI-IR,TGA,contact angle measurements and BET analysis.It was found that the surface hydrophobicity of silicalite-1 particles was improved significantly as the alkyl group was strongly bonded to the particle surface.Modified silicalite-1 particles were incorporated into PDMS(poly(dimethylsiloxanediol)) membranes,which were applied for the pervaporation separation of ethanol/water mixtures.The effect of surface properties,zeolite loading and operation conditions on pervaporation performance of the membranes was investigated.The separation factor of PDMS membranes filled with modified silicalite-1 increased considerably compared with that filled with unmodified ones,and the total flux decreased with increasing zeolite loading. The solution and diffusion selectivity of hybrid membranes were also measured to explain the pervaporation properties of silicalite-1 filled PDMS membranes.It was found that modification of silicalite-1 with dodecyltrichlorosilane effectively improved the solution and diffusion selectivity of silicalite-1 filled PDMS membranes with high zeolite loading.This may be attributed to the high surface hydrophobicity of modified silicalite-1 and its good integration with PDMS membranes.Both the high separation factor and solution selectivity indicated that modification of silicalite-1 with chlorosilanes was an effective method to improve the selectivity of silicalite-1/PDMS hybrid membranes for ethanol.     

Different viscosity grade sodium alginate and modified sodium alginate membranes in pervaporation separation of water + acetic acid and water + isopropanol mixtures

Different viscosity grade sodium alginate (NaAlg) membranes and modified sodium alginate membranes prepared by solution casting method and crosslinked with glutaraldehyde in methanol:water (75:25) mixture were used in pervaporation (PV) separation of water+acetic acid (HAc) and water+isopropanol mixtures at 30 °C for feed mixtures containing 10–50 mass% of water. Equilibrium swelling experiments were performed at 30 °C in order to study the stability of membrane in the fluid environment. Membranes prepared from low viscosity grade sodium alginate showed the highest separation selectivity of 15.7 for 10 mass% of water in the feed mixture, whereas membranes prepared with high viscosity grade sodium alginate exhibited a selectivity of 14.4 with a slightly higher flux than that observed for the low viscosity grade sodium alginate membrane. In an effort to increase the PV performance, low viscosity grade sodium alginate was modified by adding 10 mass% of polyethylene glycol (PEG) with varying amounts of poly(vinyl alcohol) (PVA) from 5 to 20 mass%. The modified membranes containing 10 mass% PEG and 5 mass% PVA showed an increase in selectivity up to 40.3 with almost no change in flux. By increasing the amount of PVA from 10 to 20 mass% and keeping 10 mass% of PEG, separation selectivity decreased systematically, but flux increased with increasing PVA content. The modified sodium alginate membrane with 5% PVA was further studied for the PV separation of water+isopropanol mixture for which highest selectivity of 3591 was observed. Temperature effect on pervaporation separation was studied for all the membranes; with increasing temperature, flux increased while selectivity decreased. Calculated Arrhenius parameters for permeation and diffusion processes varied depending upon the nature of the membrane.     

Dehydration of acetonitrile using cross-linked sodium alginate membrane containing nano-sized NaA zeolite

Pervaporation (PV) separation of water–acetonitrile mixture using sodium alginate (NaAlg) based mixed matrix membranes (MMM) comprising different amounts of nano NaA zeolite (10, 20 and 30 wt%) is investigated in various concentrations of water and temperatures. The prepared membranes are modified by sulfosuccinic acid (SSA) as a crosslinking agent. NaAlg-NaA/SSA membranes are synthesized by a solution casting technique. The process and membrane performance including separation factor, flux and activation energy of permeation are determined. Results reveal that adding of nano zeolite may lead to an increase in the flux and the separation factor of sodium alginate membrane up to 123 and 169%. In addition, using MMM in dehydration of a feed containing 30 wt% of water shows much better performance than alginate membrane. Furthermore, the activation energy of water permeation through MMM is predicted lower than sodium alginate membrane which reflects the facilitated permeation of water through MMM.     

Layered Zeolite for Assembly of Two-Dimensional Separation Membranes for Hydrogen Purification

Membrane separation is an energy-efficient and environmentally friendly process. Two-dimensional (2D) molecular sieving membranes featuring unique nanopores and low transport resistance have the potential to achieve highly permeable and selective mixture separation with low energy consumption. High-aspect-ratio zeolite nanosheets with intrinsic molecular-sieving pores perpendicular to the layers are desirable building blocks for fabricating high-performance 2D zeolite membrane. However, a wider application of 2D zeolitic membranes is restricted by the limited number of recognized zeolite nanosheets. Herein, we report a swollen layered zeolite, ECNU-28, with SZR topology and eight-member ring (8-MR, 3.0 Å×4.8 Å) pores normal to the nanosheets. It can be easily exfoliated to construct 2D membrane, which shows a high hydrogen selectivity up to 130 from natural gas and is promising for hydrogen purification and greenhouse gas capture.     

A Uniformly Oriented MFI Membrane for Improved CO2 Separation

Membrane separation of CO₂ from natural gas, biogas, synthesis gas, and flu gas is a simple and energy‐efficient alternative to other separation techniques. But results for CO₂‐selective permeance have always been achieved by randomly oriented and thick zeolite membranes. Thin, oriented membranes have great potential to realize high‐flux and high‐selectivity separation of mixtures at low energy cost. We now report a facile method for preparing silica MFI membranes in fluoride media on a graded alumina support. In the resulting membrane straight channels are uniformly vertically aligned and the membrane has a thickness of 0.5 μm. The membrane showed a separation selectivity of 109 for CO₂/H₂ mixtures and a CO₂ permeance of 51×10^?7 mol m^?2 s^?1 Pa^?1 at ?35 °C, making it promising for practical CO₂ separation from mixtures.