由酸活化高岭土制备多级纳米孔HY分子筛及其表征

由酸活化的高岭土制备了多级纳米孔HY分子筛。通过改变老化时间和晶化时间可得到最大的多级因子(HF),此时外比表面积最大而微孔孔体积变化不大。运用X射线衍射(XRD)、X射线荧光光谱、N2吸附-脱附法和NH3程序升温脱附对所得样品进行了表征。老化2 d和晶化24 h所制的纳米孔HY分子筛样品的HF值最大。样品的酸性和结晶度也随着制备条件而变化。另外,适量NaCl的嵌入对提高对所制样品的HF值、酸性和结晶度起到重要作用。通过比较样品和常规HY分子筛的XRD峰强度算得样品的结晶度。结果表明,优化合成条件可得到广泛适用于工业化的分子筛制备路线。     

纳米多级孔分子筛:简短的综述（英文）

分子筛是一种三维微孔结构的硅铝酸盐晶体,具有灵活多变的骨架和组成、较高的物理和水热稳定性、无毒、高比表面积、离子可交换性以及很低的成本等特点,因而在油品精制、石油化学、农业、水和污水处理等众多领域中用作离子交换剂、催化剂和吸附剂.尽管分子筛的应用是基于其本身的微孔结构,但微孔也导致体积较大的反应物和产物分子的传质阻力高.通过制备纳米尺度和多级孔结构的分子筛等多种手段可克服常规分子筛所具有的传质限制.人们已经开发了多种方法制备了新型的分子筛材料,并考察了它们在各种催化反应和吸附反应中的性能.在反应体系中采用这种多级孔的纳米分子筛,有可能提高催化剂的使用寿命和催化性能,抑制积碳和失活.本综述概述了多级孔分子筛和纳米分子筛的高性能及其合成方法的最新进展,讨论了每个合成方法的优缺点,简述了纳米分子筛和二级孔结构分子筛的催化应用,并与常规分子筛进行了比较.     

氩吸附法研究多级孔分子筛的孔结构

采用不同方法分别制备了双介孔分子筛、介微孔分子筛及介孔沸石材料,利用氩吸附法并结合XRD技术表征了多级孔分子筛的孔结构。探讨了适用于多级孔分子筛的孔径分布计算方法,揭示了不同类型吸附等温线与孔径分布、孔型及孔容等之间的关系。研究表明,对于多级孔分子筛、微孔和介孔的孔径分布分别用SF法和BJH法计算较适宜,全孔分析可用NLDFT法计算。通过对TS-1介孔沸石的孔结构分析发现, TPAOH 在改性制备介孔TS-1的过程中起到了生成介孔及促进二次晶化的双重作用。     

多级孔钛硅分子筛的制备及应用进展

以钛硅分子筛(TS-1)为催化剂的选择性催化氧化工艺具有反应条件温和、产物选择性高及环境污染小等特点,促进了烃类催化氧化反应的绿色化发展.但常规TS-1分子筛狭窄的孔道限制了其在大分子催化氧化反应中的应用.多级孔TS-1分子筛为包含不同尺度的孔道结构的晶体沸石,兼具微孔分子筛晶体优异的水热稳定性和介孔材料优异的扩散传输性能,因此其受到国内外众多专家学者的广泛关注.多级孔TS-1分子筛的制备方法很多,主要有直接合成法和后处理法,其中直接合成法包括硬模板法、软模板法和自组装法,而后处理制备主要为碱处理法.我们在对多级孔TS-1分子筛制备方法进行归纳总结的基础上,探讨不同制备方法对分子筛中钛硅物种分布、孔道结构及催化烃类选择性氧化反应性能的影响.结合目前TS-1分子筛应用现状,对其未来发展进行展望.     

以介孔分子筛为金属催化剂载体制备纳米碳管

 以不同的介孔分子筛作为金属催化剂载体,对催化合成纳米碳管进行了系统的研究,讨论了反应条件对纳米碳管纯度和产量的影响. 结果表明,不同的介孔分子筛对金属活性中心的形成、碳组分的扩散、纳米碳管的管径及形态均有明显的影响. 此外,金属的种类、状态和含量也影响纳米碳管的合成. 探索了合成高产量纳米碳管的条件,并对介孔分子筛上生长纳米碳管的特点进行了讨论.     

含有多级孔复合分子筛的复合催化剂上合成气一步制二甲醚

以Beta分子筛为核、Y型分子筛为壳层的多级孔复合分子筛(BFZ)作为甲醇脱水催化剂用于固定床中合成气一步法制备二甲醚,并与纯Y型分子筛进行了比较,研究了二甲醚合成催化反应活性与甲醇脱水催化剂孔道结构和酸性之间的关系.结果表明,复合分子筛HBFZ具有中等强度的酸性和中孔孔道结构,有利于提高合成气制备二甲醚的催化反应活性.二甲醚直接合成催化剂由工业CuO/ZnO/Al₂O₃催化剂(CZA)与分子筛(HBFZ、HY)采用机械混合方法制备;催化评价结果显示,CZA/HBFZ比CZA/HY具有更优的催化活性和稳定性.在250 ℃, 5.0 MPa 和 1 500 h^-1的反应条件下,CZA/HBFZ催化剂上CO的转化率和DME的选择性分别达到94.2%和67.9%.     

纳米多级孔Silicalite-1分子筛负载Ziegler-Natta催化剂对聚丙烯性能的影响

分子筛无机多孔材料具有特殊的孔道结构、较大的比表面积、极佳的稳定性和独特的择形选择性,是一种优异的绿色无机载体材料.本文采用具有MFI拓扑结构的纳米尺寸多级孔分子筛Silicalite-1(S-1)作为无机载体负载Ziegler-Natta催化剂.通过X射线衍射(XRD)、扫描电子显微镜及氮气吸附-脱附等表征手段研究了纳米S-1载体的理化性质,并研究了S-1载体性质对Ziegler-Natta催化剂在合成聚丙烯反应中催化性能的影响.结果表明,在丙烯聚合反应中,纳米片状无机载体S-1较大的比表面积和多级孔特性有利于提高ZieglerNatta催化剂负载量及改善传质限制;此外, S-1载体还可以起到模板导向作用,使所得聚丙烯呈现复型效应;在相同压力和反应温度下进行的丙烯聚合反应中,由于丙烯单体受多级孔S-1载体孔道结构和尺寸的择形作用及无机载体的复型效应影响,聚合产物的结晶度和全同立构指数较高,有利于提高聚丙烯产物的熔点.     

一步法合成多级孔结构ZSM-5分子筛

多级孔结构ZSM-5分子筛的合成过程复杂。利用双模板剂,通过优化晶化条件(如晶化时间与晶化温度)和Si/Al物质的量比等一步水热晶化合成了具有多级孔结构的ZSM-5分子筛,并采用XRD、N₂吸附-脱附、吡啶红外吸脱附、SEM和TEM等方法对样品的晶体结构、孔道结构、表面酸性和形貌等进行了表征。结果表明,一步法合成多级孔结构ZSM-5分子筛的适宜条件是:晶化温度160-180℃,晶化时间24-96 h,反应物组成为SiO₂/Al₂O₃/Na₂O/CTAB/TPABr/H₂O=1/x/0.4/0.05/0.12/280,(x:50-240)。其中,晶化温度160℃、晶化时间48 h和以Si/Al物质的量比50的凝胶合成的样品具有有序的介孔(平均尺寸3.60 nm)结构、较高的结晶度和较强的酸性。     

蒸汽辅助结晶法合成多级孔整体型ZSM-5分子筛

多级孔分子筛由于其高的比表面积、良好的传质性能和可调控的孔径等特性,引起了广大科研工作者的研究兴趣.近年来,通过选择性脱除骨架硅或铝,成功合成了多级孔沸石分子筛材料.但是由于骨架原子的脱除使分子筛的结晶度降低,进而使其催化效率降低.通过硬模板法(如炭黑、介孔硅球、气凝胶等),也用于合成多级孔沸石分子筛.然而,这种方法制备过程较为复杂,且成本较高.因此,亟需发展新的多级孔分子筛的制备方法.此外,在工业应用中,沸石分子筛催化剂通常需要做成整体柱状或片形以消除固定床反应器的床层压降.合成整体型沸石分子筛的传统方法是在沸石分子筛成型过程中添加SiO2和Al2O3等无机粘结剂.虽然该方法简单易行,但沸石分子筛的孔道结构容易被破坏,而且无机粘结剂的存在使分子筛活性中心的密度减少.为了解决这些问题,合成整体型多级孔沸石分子筛,不仅具有较强的机械稳定性,适应于工业,而且其多级孔道有利于分子的扩散,从而具有较高的催化活性.针对上述问题,我们以海绵作为模板,通过蒸汽辅助结晶(steam-assisted crystallization,SAC)方法,制备具有多级孔道的整体型ZSM-5分子筛.通过X射线衍射(XRD)、氮吸附脱附、扫描电子显微镜(SEM)、透射电子显微镜(TEM)、固态核磁共振和氨气的程序升温脱附(NH3-TPD)等手段对分子筛进行了结构与性质表征.XRD和固态核磁共振的结果表明,成功合成了不同Si/Al的ZSM-5分子筛.SEM和TEM结果进一步确定了合成的整体型多级孔ZSM-5分子筛(记作M-ZSM-n,n代表Si/Al的摩尔比),由于分子筛颗粒的堆积形成的介孔,海绵模板提供的固体骨架形成的大孔,分子筛本身的微孔,共同构成了微孔-介孔-大孔的整体型ZSM-5分子筛.透射电子显微镜上配备的X射线能谱仪(EDS)结果表明,分子筛中的Si和Al元素能够均匀的分布.氮吸附脱附证明所得整体型分子筛具有明显的介孔结构.NH3-TPD结果表明,不同Si/Al的整体型多级孔ZSM-5分子筛具有不同强度的酸性,其酸性强度:ZSM-5(60)相似文献   

Low-temperature selective catalytic reduction of NOx with NH3 over zeolite catalysts: A review

The selective catalytic reduction (SCR) of NO_x by NH₃ is one of the most mature technologies for NO_x treatment. Catalysts are the main factors affecting denitrification efficiency. Zeolites as low-temperature NH₃-SCR catalysts have been extensively studied in the past few years. In this work, the mechanism of zeolites for NH₃-SCR reaction was reviewed and the denitrification performances of zeolite catalysts prepared by different methods were compared. The effects of sulfur and water poisoning on zeolite catalysts in NH₃-SCR reaction were also analyzed. Several ways to address the problems in low-temperature NH₃-SCR reaction were discussed. Hopefully, this review could provide a fundamental understanding of SCR reaction on zeolite catalysts and pave the way toward similar studies to realize its commercial applications.     

One-step synthesis of hierarchical aluminosilicate aggregates using bifunctional alkanolamine as single template

Highly active, hierarchical zeolite ZSM-5 aggregates have been prepared in a one-step synthesis using alkanolamine as single template. The effects of SiO₂/Al₂O₃, pH and H₂O/SiO₂ on the aggregate morphology of the ZSM-5 nanocrystals were investigated. The obtained aggregate zeolites characterized by SEM, TEM and BET possessed significant textual porosity (up to 0.22 cm³/g), which could be tuned by the number of substituents in the alkanolamine molecules and the amount of aluminum in the synthetic mixtures. These zeolite aggregates showed high activities for Friedel–Crafts alkylations and may curtail the filtration difficulties during the synthesis and applications to some extent.     

多级孔Beta沸石合成研究进展

沸石分子筛是许多工业过程中不可缺少的催化剂。其中,Beta沸石因其具有三维大微孔结构而成为生产广泛并且具有重要工业意义的沸石材料之一。与传统微孔Beta沸石相比,多级孔Beta沸石具有更小的空间位阻,更高的传质效率等诸多优点,从而能减少其在作为催化剂时积碳的形成,从而延长催化剂的使用寿命,提高催化剂利用效率。本文以Beta沸石为代表,从“自下而上”（直接合成）和“自上而下”（后期修饰）两种策略详细地介绍了多级孔沸石合成的研究进展,对硬模板剂法、软模板剂法、无介孔模板剂法、脱铝法和脱硅法进行了全面的介绍,并简要介绍了多级孔Beta沸石的特点,最后总结了各种合成方法的优点及存在的问题并对其未来发展前景进行了展望。     

Trimodel hierarchical yolk-shell porous materials TS-1@mesocarbon:Synthesis and catalytic application

Trimodal hierarchical yolk-shell materials consisting of TS-1 core and mesoporous carbon shell(YS-TS-1@MC) was successfully synthesized by using TS-1@mesosilica as hard template,sucrose as carbon source and organic base tetrapropylammonium hydroxide(TPAOH) as silica etching agent.The resultant YS-TS-1@MC contains the micropores(0.51 nm) in TS-1 core,the mesopores(2.9 nm) in carbon shell as well as a void or a stack pore between TS-1 fragcments(TS-1 intercrystal mesopores,～18.4 nm).Under the rigorous etching conditions,the crystalline structure of TS-1 core was well retained.The YS-TS-1@MC served as a good support for palladium nano-particles(Pd NPs) or Rh(OH)x species,giving rise to efficient bifunctional catalysts for the tandem reactions including one-pot synthesis of propylene oxide or amides.     

Hierarchical LTL Zeolite as an Efficient and Sustainable Solid Acid Catalyst for Replacing HCl in the Production of Polyurethane Intermediates

In many industrially important reactions, caustic mineral acid catalysts have been successfully replaced with green solid acids such as zeolites. In this context, extensive efforts have been devoted to replacing HCl to produce methylenedianiline (MDA), a key intermediate in polyurethane production. Unfortunately, limited success has been achieved thus far due to low activity, selectivity towards the desired 4,4′-MDA, and rapid catalyst deactivation. Here we report that meso-/microporous hierarchical LTL zeolite exhibits unprecedentedly high activity, selectivity, and stability. The one-dimensional cage-like micropores of LTL promote the bimolecular reaction between two para-aminobenzylaniline intermediates to selectively produce 4,4′-MDA and inhibit the formation of undesired isomers and heavy oligomers. Meanwhile, the secondary mesopores alleviate mass transfer limitations, resulting in a 7.8-fold higher MDA formation rate compared to solely microporous LTL zeolite. Due to suppressed oligomer formation and fast mass transfer, the catalyst exhibits inappreciable deactivation in an industrially relevant continuous flow reactor.     

Studies on the formation of hierarchical zeolite T aggregates with well-defined morphology in different template systems

In this paper, the disk-like and pumpkin-like hierarchical zeolite T aggregates consisted of primary nano-grains have been hydrothermally synthesized with and without the aid of the second template. The first template is used with tetramethylammonium hydroxide (TMAOH) and the second template is used with triethanolamine (TEA) or polyving akohol (PVA). A combination of characterization techniques, including XRD, SEM, TEM and N₂ adsorption–desorption to examine the crystal crystallinity, morphology and surface properties of hierarchical zeolite T aggregates. In the single-template preparation process, the two-step varying-temperature treatment has been used to improve the meso-porosity of zeolite T aggregates. In the double-template preparation process, the amounts of PVA or TEA on the crystallinity, morphology and meso-porosity of zeolite T aggregates have been studied. It has been proved that the interstitial voids between the primary grains of aggregates are the origin of additional mesopores of samples. The micro- and meso-porosities of samples prepared with and without the second template have been contrasted in detail at last. In particular, the sample synthesized with the addition of PVA presents a hierarchical pore structure with the highest S_ext value of 122 m²/g and V_meso value of 0.255 cm³/g.     

Application of nanosized zeolites in methanol conversion processes: A short review

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Bread-template synthesis of hierarchical mesoporous ZSM-5 zeolite with hydrothermally stable mesoporosity

A hierarchical mesoporous ZSM-5 zeolite has been synthesized by using starch-derived bread as a meso-template. The obtained mesoporous ZSM-5 was characterized with X-ray diffraction (XRD), nitrogen sorption, scanning electron microscopy (SEM), transmission electron microscopy (TEM) and thermogravimetric (TG)/differential thermal analysis (DTA) techniques. Hydrothermal treatments revealed that the mesoporosity in hierarchical mesoporous ZSM-5 exhibited excellent hydrothermal stability. Catalytic tests showed that hierarchical mesoporous ZSM-5 was more active than conventional zeolite of ZSM-5 in catalytic cracking of 1,3,5-tri-isopropylbenzene. Hydrogen adsorption measurements showed hierarchical mesoporous ZSM-5 had a higher storage capacity than the conventional ZSM-5.     

On the structures of X- and Y-type zeolites. Structural changes within the cavities of Na-Y during dehydration and contrasts with Na-X systems

Samples of dehydrated and partially dehydrated Na-Y were examined by X-ray diffraction methods revealing the progressive structural changes which occur as water is removed and the different behaviour compared with Na-X. The differences between Na-Y and Na-X reflect the reduced Al content of Na-Y and the consequential lower average capability of each framework oxygen atom for balancing cation charges. In the small-pore region of Na-Y, the total number of Na atoms remains relatively constant during dehydration (ca. 15 per unit cell compared withca. 18 in Na-X); unlike Na-X, Na-Y, has no site I atoms. Significant dehydration of the small-pore region, and the change from low to high site II occupancy, do not occur until the total water content of the sample is less than that which pertains under atmospheric conditions. In the 12-ring regionn of Na-Y, [Na(H₂O)₂]⁺ units are observed at an intermediate level of dehydration, possibly linked by water molecules astride the site III region to networks in adjacent 12-rings. There is no build-up, as in Na-X, of Na at site III, and site IIB (=III) is (at least partially) occupied by H₂O rather than Na. Further dehydration progressively removes H₂O but there is little rearrangement of Na atom positions, except the build-up in site II which accounts for much of the loss of Na from the mobile phase.