SSZ-13分子筛膜的制备方法及其气体分离

SSZ-13分子筛具有CHA构型和3维八元环孔道结构,窗口尺寸约0.38 nm×0.38 nm。相比CH₄和N₂,SSZ-13分子筛对CO₂具有优先吸附选择性,适用于CO₂/CH₄、CO₂/N₂等体系的气体分离。SSZ-13分子筛膜的制备方法主要有原位晶化法、二次生长法、微波合成和分子筛转晶法等。高硅SSZ-13分子筛膜的疏水性随着硅铝比的增加而增加,膜层变得更加致密,缺陷减少,气体分离选择性增加。本文梳理了高硅SSZ-13分子筛膜的制备方法和气体分离的机理,分析了支撑体、合成条件、Si/Al比、测试条件和分离体系等因素对高硅SSZ-13分子筛膜气体分离的影响,展望了高硅SSZ-13分子筛膜今后的发展方向。     

预吸附微波合成纳米NaY沸石晶种制备NaY型分子筛膜

在常压回流的微波加热体系中成功地合成出纳米尺寸的NaY分子筛,XRD和SEM等表征结果表明,分子筛具有40nm左右的平均晶粒尺寸.以其为晶种,预吸附在多孔氧化铝载体上,结合原位水热法进行二次晶化,制备出较为致密的NaY分子筛膜,该膜主要以孪生聚晶的形式存在.CO₂/N₂气体分离测试结果显示,随着温度的升高,分子筛膜的气体分离能力呈上升趋势,在140℃时真实选择分离系数达到最大值4.0.     

多孔载体上纯相MgAPO-36和CoAPO-36分子筛膜的合成与表征

<正>分子筛膜具有与常见气体和溶剂分子大小相当的规则孔道结构,良好的热稳定性和催化性能,可用于强化气体混合物分离[1-2]和膜反应过程[3-4]。到目前为止,沸石分子筛膜(如BEA、LTA和MFI型)和磷铝分子筛膜(如AEI、AFI和CHA型)相关的研究工作均有大量报道[5],但ATS型磷酸铝分子筛薄膜的合成与应用研究仍未见公开报导。     

二维纳米片用于快速高效膜法气体分离

膜法气体分离作为一类低能耗先进分离技术, 在化工分离中具有广阔的应用前景. 然而商业气体分离膜在实际应用过程中存在选择性和渗透性此消彼长的问题. 以二维纳米片材料为膜构筑基元, 有望突破这一瓶颈. 最具代表性的二维纳米片膜材料当属石墨烯及其衍生物、 二维沸石分子筛、 层状双金属氢氧化物、 二维过渡金属硫化物、 Mxene、 二维共价有机骨架和金属有机骨架材料. 本文对这些二维材料在超薄气体分离膜领域的成果与进展进行介绍, 展现了各类材料在实际分离应用过程中的优势及弊端, 探讨了二维纳米片膜材料在气体分离领域的挑战与发展前景.     

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。     

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。     

MFI型分子膜的制备与H2S/CH4分离性能

采用二次生长法在多孔α-Al₂O₃载体上制备MFI型（ZSM-5和silicate-1）分子筛膜;通过XRD和SEM检测,证明所合成的分子筛膜为致密、交联和无取向的MFI型分子筛膜,厚度为5 μm;单组分气体渗透实验检测中,所制备样品膜的N₂渗透量均小于10^-11 mol/（m²·s·Pa）,可认为其无缺陷;同时,考察了样品分子筛膜对H₂S/CH₄混合气的分离效果,在渗透压分别为0.3和0.5 MPa时,silicate-1分子筛膜的H₂S/CH₄的分离因子分别为1.99和4.44,而ZSM-5分子筛膜的CH₄/H₂S的分离因子分别为6.71和12.85。     

ZSM-5分子筛膜的研究进展

本文分析了ZSM-5分子筛膜的主要合成方法和研究现状,总结了ZSM-5分子筛膜的缺陷与修饰方法,指出了ZSM-5分子筛膜的表征手段是以XRD、SEM、TEM和单组分气体渗透等为主,对ZSM-5分子筛膜的应用和前景进行了展望.     

ZSM-5分子筛膜的研究进展

本文分析了ZSM-5分子筛膜的主要合成方法和研究现状,总结了ZSM-5分子筛膜的缺陷与修饰方法,指出了ZSM-5分子筛膜的表征手段是以XRD、SEM、TEM和单组分气体渗透等为主,对ZSM-5分子筛膜的应用和前景进行了展望。     

ZSM-5分子筛膜的研究进展

本文分析了ZSM-5分子筛膜的主要合成方法和研究现状，总结了ZSM-5分子筛膜的缺陷与修饰方法，指出了ZSM-5分子筛膜的表征手段是以XRD、SEM、TEM和单组分气体渗透等为主，对ZSM-5分子筛膜的应用和前景进行了展望。     

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.     

膜分离天然气脱水蒸汽技术的研究现状

天然气脱水蒸汽是天然气净化过程中的必要环节,选择合适的脱水蒸汽技术和工艺至关重要。本文首先简要概述了新兴的膜分离天然气脱水蒸汽方法的特点,然后介绍了膜分离性能的表征参数及测试、膜组件设计及操作条件的选择,重点介绍了近年来膜分离甲烷脱水蒸汽技术中的聚合物膜材料、沸石分子筛膜材料,最后展望了金属有机骨架材料的应用潜力以及天然气脱水蒸汽技术未来的发展趋势。     

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.     

Synthesis Optimization of SSZ-13 Zeolite Membranes by Dual Templates for N2/NO2 Separation

High-silica SSZ-13 zeolite membranes are promising in industrial separations of light gases and continuous membranes are highly demanded for better separation performances. Herein, pure-phase, continuous and thin SSZ-13 zeolite membranes were synthesized using dual templates of N,N,N-trimethtyl-1-adamantammonium hydroxide(TMAdaOH) and tetraethylammonium hydroxide(TEAOH). Systematical investigations of TMAdaOH/TEAOH ratios and their concentrations show that TMAdaOH acts as the main structure-directing agent in the formation of the SSZ-13 zeolite. TMAdaOH cooperatively plays with TEAOH in promoting the SSZ-13 crystal intergrowth to form a continuous polycrystalline membrane. Additionally, appropriate introduction of TEAOH is able to adjust the membrane thickness to the crystal-comparable size of ca. 2.0 μm. The SSZ-13 membranes are further applied for N₂/NO₂separation, which is firstly reported on zeolite membranes. The gas permeation results show that the SSZ-13 membrane synthesized by the dual-template approach exhibits selective separation of N₂ over NO₂ with N₂/NO₂ separation factor of 7.6 and N₂ permeance of 1.66×10^-8 mol·m^-2·s^-1·Pa^-1.     

不锈钢金属网上L型分子筛膜的连续生长及气体渗透性能

选取不锈钢金属网作为成膜载体, 采用预涂晶种的方法, 研究了L型分子筛晶种在水热条件下二次生长成膜的过程. 对成膜条件进行了详细的考察, 并讨论了反应液的碱度及反应时间对L型分子筛膜形成的影响. 利用扫描电子显微镜(SEM)对L型分子筛膜的形貌进行了表征. 通过优化反应条件, 得到了致密、 连续、 纯相、 均匀的L型分子筛膜, 厚度约为20 μm. 单组分气体渗透测试结果表明, 在室温和常压下, L型分子筛膜对N₂气和H₂气的渗透速率分别为8.39×10^-8 和6.96×10^-7 mol·m^-2·s^-1·Pa^-1, 从而计算出膜对H₂/N₂混合气体的理想分离系数为8.3. 双组分气体渗透测试结果表明, 温度的升高会导致膜对H₂气和N₂气的渗透速率增加及H₂/N₂分离系数的减小.     

Improving the Gas-Separation Properties of PVAc-Zeolite 4A Mixed-Matrix Membranes through Nano-Sizing and Silanation of the Zeolite

Mixed-matrix membranes containing synthesised nano-sized zeolite 4A and PVAc were fabricated to investigate the effect of zeolite loading on membrane morphology, polymer-filler interaction, thermal stability and gas separation properties. SEM studies revealed that, although the membranes with 40 wt % nano-sized zeolite particles were distributed uniformly through the polymer matrix without voids, the membranes with 15 wt % zeolite loading showed agglomeration. With increasing zeolite content, the thermal stability improved, the permeability decreased and the selectivity increased. The effect of silanation on dispersion of 15 wt % zeolite 4A nanoparticles through PVAc was investigated by post-synthesis modification of the zeolite with 3-Aminopropyl(diethoxy)methylsilane. Modification of the nanoparticles improved their dispersion in PVAc, resulting in higher thermal stability than the corresponding unmodified zeolite membrane. Modification also decreased the rigidity of the membrane. Partial pore blockage of the modified zeolite nanoparticles after silanation caused a further decrease in permeability, compared to the 15 wt % unmodified zeolite membrane.     

CO2／CH4分离膜及沸石填料影响渗透过程的研究

报导了甲基硅橡胶和纤维素（ＣＡ、ＣＴＡ、ＥＣ）膜对ＣＯ２、ＣＨ４的选择透气性能，并讨论了沸石作为填料所引起的分子筛作用的气体渗透过程。甲基硅橡胶的气体渗透系数最高，而选择性最低，且不受填料沸石的影响。纤维素膜的气体选择性较大，渗透系数可以通过沸石的加人而明显增加。特别是沸石１３Ｘ．沸石３Ａ、４Ａ、５Ａ在ＥＣ膜中对气体分子筛作用，改变了气体原有的渗透过程，提高了选择性。使用Ａｒｒｈｅｎｉｕｓ公式计算出ＥＣ－沸石３Ａ膜的气体渗透活化能。     

高硅ZSM—5沸石填充硅橡胶膜的醇—水渗透蒸发分离性质

高硅ZSM－5沸石填充疏水性硅橡胶蓦地低浓度醇－水体度醇－水体的渗透蒸发性质的研究有明，提高沸石硅铝比，增加填充量以及进行酸处理皆有利于改善膜对醇－水的分离系数和通量。料液的成，浓度以及温度对膜的分离性质也有显著影响。     

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.     

Zeolite Membranes: From the Laboratory Scale to Technical Applications

Current trends and novel concepts in R&D of zeolite membranes like the seeding supported crystallization and the preparation of Al-containing zeolite membranes are discussed. The influences of adsorption and diffusion on the permeation properties of zeolite membranes are considered. Dehydration of ethanol by steam permeation and pervaporation as the first zeolite membrane based industrial separation is presented. Membrane supported dehydrogenation and esterification are discussed as possible applications of a catalytic membrane reactors. In memoriam Wolfgang Schirmer.