澄清溶液中NaA型分子筛膜的合成及气体渗透性能

The use of zeolite membranes in separation or combined reaction and separation processes is very attractive. Advantages of using such a type of membranes include their ability to discriminate molecules based on the molecular size and their stability[1]. In the past ten years, most efforts were involved in the synthesis and permeation studies of MFI zeolite membrane[2, 3]. Recently, NaA zeolite membrane has attracted much attention because of its high potential in the dehydration of organic liquids[4]. However, few gas permeation results were reported[5]. Furthermore, most of the NaA zeolite membrane was synthesized from gel[4]. In this letter, the synthesis of NaA zeolite membrane from clear solution and its gas permeation properties are reported.     

NaA分子筛膜催化剂上CO和C2H4混合气的选择性氧化反应

Defect-free zeolite NaA membranes were coated onto the surface of spherical Pt/Al2O3 particles using a two-step hydrothermal method. The structure and morphology of the synthesized composite catalysts were characterized using XRD and SEM techniques, respectively. The results indicated a layer of compact and uniform NaA molecular sieve membrane with a thickness of about 20 滋m was coated on the spherical Pt/Al2O3 particles after the two-step hydrothermal synthesis. The prepared NaA membrane coated catalysts were used in the oxidation of a mixture of CO and C2H4 to study the reactant selectivity over the coated zeolite NaA membranes. Under the optimized conditions, the oxidation selectivity for CO over C2H4 on the composite catalyst was as high as 96%. The feasible application of this composite membrane coated catalyst to the selective removal of CO in the presence of C2H4 was anticipated.     

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.     

在多孔γ-Al2O3氧化铝载体上微波合成NaA分子筛膜及气体渗透分离性能

The paper presented novel synthesis of NaA zeolite membrane with good performance using microwave heating. The method involved two steps, prior seeding 120 nm of LTA crystals on substrate and then employing a secondary hydrothermal synthesis. Effects of seeding times, synthesis time and synthesis times were investigated in this work. The quality evaluation of membranes respectively used single component gases (HE and N2) and H2/N2 (equivalent volume) mixture. The ideal H2,/N2 selectivity increased from 1.90 of the substrate to 6.37 of the three-stage synthesized membrane, which was distinctly higher than the corresponding Knudsen diffusion selectivity of 3.74. However, the real H2/N2 selectivity of the three-stage synthesis was much lower than the corresponding ideal selectivity and close to the corresponding Knudsen diffusion selectivity of 3.74.     

用无机硅钛原料合成无铝Ti-β分子筛的研究

Ti-β zeolite has been successfully synthesized by using fumed silica and TiCl₃ as silicon and titanium sources respectively under the hydrothermal conditions.Because inorganic Si and Ti compounds instead of relative organic metal compounds were used in the synthesis of Ti-β ,and then a tedious hydrolysis procedure of organic metal compounds was avoided,the gelatin time was reduced,the synthesis process was simplified and easily reproduced.Importantly,the synthesized Ti-β zeolite,which was characterized by XRD, FT-IR, UV-Vis and DTA, didn't exist TiO₂ crystals and had a good quality.     

含氟体系中DDR型分子筛的合成

DDR (Deca-dodecasil 3R) zeolite was synthesized hydrothermally in fluoride medium. The effects of synthesis conditions including the amount of KF, different fluoride sources and seeds on crystallization of DDR zeolite were investigated. The as-synthesized DDR zeolite samples were characterized by X-ray diffraction (XRD) and scanning electron microscope (SEM). The results demonstrated that DDR crystallization was strongly affected by n_KF/n_SiO2, fluoride sources and seeds. Pure DDR zeolite could be successfully obtained in n_KF/n_SiO2 range of 0.5～1 after 9 days of hydrothermal synthesis. The synthesis time was reduced to 1 day by adding small amount of seeds with yield approaching 100%.     

银离子与聚酰胺-胺型树形高分子配位作用的研究

The complexation between poly(amidoamine) (PAMAM) dendrimers and silver ion was studied in this paper. The results showed that generations and surface groups of dendrimers， reaction time， pH value， mole ratio of Ag⁺/PAMAM dendrimers， as well as reaction temperature strongly influence complexation between Ag⁺ and PAMAM dendrimers. The maximum complexing number of Ag⁺ that amino-， hydroxyl- and carboxylate- terminated PAMAM dendrimers could bind has been obtained. It has been found that the measured value of amino- and hydroxyl- ter-minated PAMAM is almost similar to the theory value， but to carboxylate- terminated PAMAM， there is a dis-crepancy between the measured value and theory value because of the electrostatic interaction between the silver ion and carboxyl group.     

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     

ZSM-5沸石膜的吸附表征

The framework and thickness of synthesized ZSM-5 membranes were characterized using static and dynamic adsorption methods. It is shown that the adsorptive properties of the membranes are the same as ZSM-5 zeolite, the average thickness of the membranes was 13 μm calculated from the adsorptive ability, which matched very well with the result measured by scanning electron micrograph. The results also shown that zeolite membranes have greated adsorptive ability than zeolite powders. The high Si/Al rate zeolite membranes have selective ability on ethanol/water, and this interpreted the separation of ethanol-water mixtures with the membranes.     

Preparation of Three Dimensional Hydroxyapatite Nanoparticles/Poly(vinylidene fluoride) Blend Membranes with Excellent Dye Removal Efficiency and Investigation of Adsorption Mechanism

In this work, poly(vinylidene fluoride)(PVDF) membranes with hydrophilicity as well as preeminent mechanical strength and dye removal efficiency were fabricated by blending with three dimensional hydroxyapatite nanoparticles(HAPNPs). Surface chemical composition and morphology of the prepared membranes were systematically investigated by ATR-FTIR, XPS, XRD, FESEM, and EDS mapping analyses. The results verified that a large number of HAPNPs were successfully embedded on the modified membrane crosssections. Moreover, HAPNPs content in the casting solution is an important factor that could have profound influence on the structures and performances of PVDF/HAPNPs blend membranes. The optimal membrane M2 with 2 wt% HAPNPs exhibited excellent hydrophilicity, outstanding mechanical strength of 19.60 MPa, and high water flux of(2466 ± 31) L·m~(–2)·h~(–1). The maximum static adsorption capacity of the optimal membrane was about 10.83 mg/g, which is 3.75 times that of the pristine PVDF membrane(2.89 mg/g).PVDF/HAPNPs membranes were not only utilized for static adsorption, but also applied to dynamic dye removal. The possible adsorption mechanism between Congo red(CR) and HAPNPs embedded on the blend membranes was firstly discussed in this work. HAPNPs interacted with CR via Lewis reaction, hydrogen bond interaction, as well as electrostatic attraction to achieve the adsorption effect.Herein, the PVDF/HAPNPs blend membranes with extraordinary hydrophilicity, mechanical strength, and dye removal efficiency possess tremendous potential for practical applications of wastewater treatment.     

预涂布晶种法合成无缺陷A型分子筛膜的研究

采用一种颗粒度约为200nm的胶态A型分子筛为晶种源,对晶种层进行特殊的蒸气处理后,进一步采取原位水热晶化法,在多孔氧化铝载体表面制备出A型分子筛膜。膜分子筛以特殊的孪生聚晶形式生长在一起,可有效地消除晶粒间隙,形成致密的分子筛膜层。晶化反应液的碱度对A型分子筛膜的质量影响很大,低碱度更有利于A型分子筛膜的生长。在对分子筛膜进行高温活化处理过程中产生一些缺陷孔,降低了膜气体分离性能。     

Synthesis of Zeolite ZSM-2 Using Zeolite NaX as Seeds

Introduction Oxygen and nitrogen have been produced tradition-ally by cryogenic distillation of air. Methods for the non-cryogenic separation based on selective adsorption have been developed and commercialized since the 1970s and have led to a cost-effective process for this important separation.1 Low-silica zeolites are important materials for producing oxygen by selective adsorption of nitrogen. In 19891990, a new generation of lith-ium-based adsorbents was developed.2,3 Highly lithium exc…     

A型分子筛膜的研究进展*

本文简述了分子筛膜的发展概况, 总结了A 型分子筛膜的制备方法、制备过程中各种因素对成膜的影响、A 型分子筛膜的形成机制, 并对评价分子筛膜的手段(XRD、SEM、气体渗透) 和A 型分子筛膜的应用(渗透汽化、膜催化) 进行了分析。     

偏高岭土水热合成4A沸石晶化行为的研究

以偏高岭土为原料合成4A沸石,由于其合成过程工艺简单,成本低而一直受到普遍的关注,对于该法晶化过程的行为研究,近年来陆续出现报道,Rocha等^[1]研究认为偏高岭土在碱液中缓慢溶解,形成含SiO3^2-,SiOH基团和Al(OH)4^-的溶液,逐步缩合为硅铝酸钠凝胶,再进一步形成4A沸石晶粒并通过结构重排而转变为4A沸石,王建等^[2]研究提出偏高岭土在NaOH溶液中部分溶解,且迅速转变为偏高岭土,并伴有硅铝酸钠凝胶产生,同时偏高岭土也不断在碱液的作用下凝胶化,生成的凝胶再进一步转变为4A沸石,因而合成的4A沸石产品与化学合成法存在着较大的差异。对偏高岭土合成4A沸石的晶化历程,作者曾进行过研究^[3],发现偏高岭土在碱液中溶解很小,由偏高岭土转为4A沸石晶型,主要是在偏高岭土固相的基础上进行的。本文似从合成过程的机理方面,探讨偏高岭土合成4A沸石的晶化过程行为及其与化学法合成产品差异的关键所在。     

NaA型分子筛膜的合成及分离性能的研究

在自制的片状多孔陶瓷载体上,通过多次原位水热晶化合成出ＮａＡ型分子筛膜,通过扫描电子显微镜观测,发现在某些区域,小颗粒的ＮａＡ型分子筛以非常紧密的形式畸晶孪生在一起,其致密度远好于由分子筛晶粒松散无规律堆积而形成的膜排列经类膜生长形式可能是获得取致密无缺陷型分子筛膜的一种途径,单组分及双组分气体渗透测试结果表明,在所合成的分子筛膜上,晶粒间隙孔可能是主要的膜扩散通道,可凝聚气体异丁烷因发生毛细管凝     

以两种季铵碱为模板剂合成A形体富集Beta沸石及其晶化过程

以三甲基环己基氢氧化铵和二甲基乙基环己基氢氧化铵为模板剂或结构导向剂(SDA), 采用超浓水热方法合成了A形体富集的Beta沸石, 用粉末X射线衍射(XRD)、 扫描电子显微镜(SEM)、 ²⁹Si固体魔角自旋核磁共振(²⁹Si MAS NMR)以及氮气吸附等表征手段对其进行了详细表征, 探索了最优合成条件, 研究了其晶化过程. 结果表明, 在晶化初期产物中己出现A形体过量特征, 随着晶化的进行, A形体的过量程度无显著变化.     

环境友好助洗剂——4A沸石

介绍了4A沸石的结构、性质及其作为洗涤助剂等方面的应用和国内外发展状况。     

超声波合成磁性4A沸石分子筛

为了解决微细粉末状沸石产品应用中与所处理溶液难以分离的问题, 在传统水热合成法合成4A沸石的晶化原料液中, 加入磁性Fe3O4微粒, 经过70 ℃, 功率为100 W的超声波晶化6 h, 合成了一系列Fe3O4含量不同的磁性4A沸石,并对其进行了XRD、SEM、IR、TG/DTA、EDX、磁化率及吸附性能等表征测试. 结果表明, 磁性4A沸石具有良好的磁稳定性, 其磁化率随Fe3O4含量的增加而增大; 磁性4A沸石对水中氟离子和六价铬的吸附与纯4A沸石性能相同, 其吸附速率可以用拟二级动力学方程来描述.     

偏高岭土合成4A沸石机理的研究

用XRD、FT IR、ICP、SEM、化学分析等方法研究了偏高岭土合成4A沸石的晶化反应机理。偏高岭土在NaOH溶液中部分溶解 ,且结构迅速转变为偏高岭土 * ,并伴有硅铝酸钠凝胶形成。偏高岭土 *也不断在碱液的作用下凝胶化 ,生成的凝胶进一步再转变为4A沸石 ,这两个过程在大部分反应时间里是同时进行的 ,直到晶化结束。液相参与凝胶、4A沸石前驱及晶核等的形成和4A沸石的成长。偏高岭土 *的凝胶化速度是整个晶化过程的决定步骤 ,该晶化过程极易形成大量聚晶。