MD模拟研究MFI沸石晶体双模板剂择优生长机理

以分子动力学(MD)方法模拟研究双模板剂在全硅MFI型沸石b轴择优取向晶体定向生长过程中的作用机制. 分别以全硅晶格模型和切面模型, 模拟两种模板剂分子(正丙胺、六亚甲基四胺)各自在孔道交叉笼内和孔道开口处的动力学行为, 考察其动力学吸附位置以及与沸石孔壁的尺寸匹配作用. 计算表明, 正丙胺分子对MFI晶体的形成和生长起主要导向作用, 而六亚甲基四胺分子有利于晶体沿a轴方向的晶面生长, 却阻碍沿b轴方向的晶面生长.     

高岭土原位无溶剂法合成小粒径ZSM-5分子筛

结合原位水热法和无溶剂法的优点,在不添加有机模板剂和溶剂的基础上,以高岭土为原料通过晶种诱导绿色高效地合成出ZSM-5分子筛。运用X射线衍射、N2吸附-脱附、扫描电镜、透射电镜和NH3程序升温脱附(TPD-NH3)等技术对ZSM-5分子筛进行表征。表征结果与原位水热法合成的ZSM-5分子筛相比,原位无溶剂法合成ZSM-5分子筛的结晶度较高、晶体粒径较小、酸强度略高、孔结构相似。     

单一模板线性多胺一步合成多级孔ZSM-5沸石微球

线性多胺模板剂(二乙烯三胺(DETA)、三乙烯四胺(TETA)、四乙烯五胺(TEPA))作为单一模板合成了均匀的10-15 μm的多级孔沸石ZSM-5微球. 实验发现, 在水热过程中, 50 nm纳米的沸石晶体粒子自发地堆积成微球, 并且这些微球具有较大的介孔体积, 在傅-克烷基化反应中具有高的催化活性. 同时,我们发现线性多胺起到了模板剂和空隙填充剂的多重功能,这点明显不同于以前我们报道的线性二胺作为模板剂在合成ZSM-5沸石时,主要是起模板剂的作用.     

晶种导向下干胶法合成ZSM-5分子筛

以廉价水玻璃为硅源,在晶种替代有机模板剂的条件下采用干胶法合成了ZSM-5分子筛。利用XRD、SEM、TEM、FTIR、N_2吸附-脱附和NH_3-TPD等分析方法对合成样品进行了表征和测试,考察了合成条件对ZSM-5分子筛晶化过程的影响。结果表明,在硅铝比(n/n)为30~70,钠硅比(n/n)为0.12~0.20时都可以得到结晶度良好的ZSM-5分子筛。研究发现,干胶法合成ZSM-5,在不引入外加水的情况下也可以得到ZSM-5样品,外加水的引入能够有效地提高晶化速率;与水热法合成ZSM-5分子筛相比,干胶法可以显著地缩短晶化时间,同时,合成样品的晶体尺寸也有所减小。     

高硅分子筛ZSM-23的合成及表征

采用静态水热晶化法以吡咯烷为模板剂,合成出结晶度良好的ZSM-23分子筛晶体.对合成条件的研究结果表明,合成的关键是避免ZSM-35分子筛的生成.当n(Si)/n(Al)=25～110,n(H20)/n(SiO2)=1.3～4.8,n(pyr.)/n(SiO2)=0.12～0.5时,均能稳定生成ZSM-23分子筛晶体.当n(Si)/n(Al)>110时,不能得到分子筛晶体;当n(Si)/n(Al)<25时,生成的是ZSM-35分子筛晶体.采用XRD,SEM,TG-DTA,FTIR等技术,对合成的ZSM-23分子筛晶体的形貌,以及影响分子筛合成的因素进行了详细的研究.     

以一种新型Gemini表面活性剂作为介孔模板剂通过转晶过程合成介孔ZSM-5分子筛

将一种新型Gemini表面活性剂,丙撑基双(十八烷基二甲基氯化铵)[C18H37(CH3)2–N+–(CH2)3–N+–(CH3)2C18H37]Cl2(C18-3-18),作为介孔模板剂用于水热法合成介孔ZSM-5分子筛.结果表明,在130 oC低温晶化即可高效合成介孔ZSM-5分子刷.C18-3-18的加入量可影响到所合成介孔ZSM-5分子筛的相对结晶度和织构性质,它的形成遵从一个转晶过程.在合成初期,凝胶中介孔模板剂C18-3-18的使用导向了介孔材料的生成;随后在TPABr的模板作用下,介孔材料慢慢转晶生成具有MFI结构的介孔ZSM-5;然后所合成的介孔ZSM-5晶粒进一步长大并聚集形成块状颗粒,同时产生晶间介孔.C18-3-18作为介孔导向剂不仅可用于合成介孔ZSM-5分子筛,也可用于其它介孔分子筛的合成中.     

丙烯在ZSM-5沸石上齐聚反应的研究Ⅰ. 模板剂用量对丙烯齐聚反应的影响

考察了不同正丁胺(NBA)模板剂用量合成ZSM-5沸石的物化特性和催化性能.采用XRD、SEM、NH3-TPD和BET等手段对合成样品的物化特性进行了表征.结果表明,模板剂与SiO2摩尔比在0.67～0.22时合成的ZSM-5沸石结晶度高于90%;随着模板剂用量的减少,ZSM-5沸石的平均粒径减小,强酸量也存在相同的趋势.丙烯齐聚反应评价结果显示,模板剂用量对合成ZSM-5沸石的催化活性有显著影响,模板剂与SiO2摩尔比在0.67～0.45之间合成的沸石催化性能较好.     

加压毛细管电色谱法分离1-甲基-3-苯基丙胺对映体

运用毛细管电色谱(pCEC)模式,以羟丙基-β-环糊精(HP-β-CD)作为手性选择剂,对1-甲基-3-苯基丙胺对映体进行手性分离。1-甲基-3-苯基丙胺对映体在最佳的条件下如:手性选择剂浓度10g/L、流动相配比:V(乙腈)∶V(磷酸盐体系)=60∶40溶液(5mmol/L)、背景电解质pH=7.6、柱温16℃和分离电压10kV达到了基线分离,该方法重现性好、简便、快捷。     

无模板剂条件下ZSM-5与丝光沸石之间的可控转晶

采用预晶化液添加法,即将高温(190oC)预晶化液添加到低温(150oC)晶化母液中合成沸石分子筛,考察了高温预晶化液的Na2O:SiO2比、预晶化时间以及低温晶化母液的Na2O:SiO2比对ZSM-5与丝光沸石之间转晶的影响,并采用X射线衍射和扫描电子显微镜对合成的产物进行了表征.研究发现,通过调节整体合成液的Na2O:SiO2比可有效控制ZSM-5沸石与丝光沸石之间的转晶.当整体合成液的组成为xNa2O:100SiO2:2.5Al2O3:12SO42?:4000H2O时,Na2O:SiO2=0.18是ZSM-5沸石和丝光沸石的一个分界线.通过调节母液的Na含量,使Na2O:SiO2>0.18时,高温预晶化过程中产生MFI结构的晶体在低温晶化时可向丝光沸石发生转晶;当Na2O:SiO2≤0.18时,具有MFI和丝光沸石结构共生的晶体在低温晶化时向MFI结构的ZSM-5沸石发生转晶.ZSM-5与丝光沸石之间转晶的前提条件是高温预晶化所形成晶体的结晶度不能太高(≤30%).另外,整体合成液中Na2O含量对生成晶体的形貌也有影响.     

低温加氢裂解脱除高硅ZSM-5分子筛内TPAOH模板剂

分子筛膜的合成和应用是近年来的研究热点, 特别是具有独特孔道结构的MFI 型分子筛膜. 但由于膜内有机模板剂在高温脱除时会导致膜产生缺陷, 进而影响分子筛膜的应用. 所以分子筛膜及分子筛晶体中有机模板剂的低温脱除工艺一直是研究者们致力解决的问题之一. 本文系统考察了高硅ZSM-5分子筛晶体内有机模板剂(四丙基氢氧化铵, TPAOH)在H₂/N₂气氛下的低温裂解脱除规律, 采用低温加氢裂解工艺, 在350 ℃以下可有效脱除分子筛晶体孔道内的有机模板剂. 通过对裂解后分子筛晶体的比表面积(BET)、热失重(TG)、傅里叶变换红外(FTIR)光谱和拉曼光谱表征证实, 相比于空气和氮气气氛, 含氢还原性气氛更有利于模板剂的低温脱除, 脱除率随温度的升高而增加; 280 ℃时, 加氢裂解后晶体的BET比表面积已达到252 m²·g^-1, 仍有少量有机残余物; 350 ℃时, 加氢裂解后晶体的BET比表面积可达到399 m²·g^-1, 仅有微量无机碳残余物. 此外, 低温加氢裂解后的分子筛表面相对洁净, 且氨气程序升温脱附(NH₃-TPD)结果表明低温加氢裂解后的ZSM-5 分子筛晶体具有相对较多的酸性位.     

Preparation of a Completely Oriented Molecular Sieve Membrane

Growth of oriented seed crystals on a substrate led to a completely oriented and continuous membrane of LTA-type zeolite. The seed crystals of cubic morphology were dip-coated onto a tilted substrate (see schematic diagram) with the zeolite channels normal to the surface. The substrate was hydrothermally treated in a reaction mixture containing the organic ligand 2,2-bis(hydroxymethyl)-2,2',2"-nitrilotriethanol, which lowers the degree of supersaturation of [Al(OH)(4)](-) ions and preferentially facilitates the intergrowth of the seed crystals.     

Alcohol-Assisted Synthesis of Sheet-Like ZSM-5 Zeolites with Controllable Aspect Ratios

Sheet-like ZSM-5 has been regarded as a promising material for catalytic applications due to its diffusion superiority. However, it still remains a challenge to obtain a desirable sheet-like morphology because of the complex synthesis process of zeolites. Here, a facile strategy for synthesizing sheet-like ZSM-5 is developed by only adding ethanol as zeolite growth modifier in the synthesis gel. It is thought that ethanol might be preferentially absorbed on the {010} surface of zeolite crystals, interact with the exposed silicon hydroxyl groups on the crystal {010} facet, and suppress the growth of b axis, resulting in the sheet-like shape. Through finely tunning synthesis parameters, sheet-like ZSM-5 crystals with thin b-axis thickness of 90 nm and different aspect ratios could be obtained. Owing to its shorter diffusion path and optimized acidity, sheet-like ZSM-5 exhibits better catalytic performance than conventional ZSM-5 in the alkylation of benzene with ethanol.     

不同形貌ZSM-5分子筛的制备及其催化甲醇转化制烯烃性能

采用廉价的原料,通过添加尿素及调节碱度,在水热条件下合成了具有不同形貌的ZSM-5分子筛。研究了分子筛形貌对甲醇转化制丙烯催化性能的影响。结果表明,通过控制尿素含量及碱度,可以对ZSM-5分子筛晶体的生长方向及形貌进行调控。当urea/SiO₂(mol ratio)=0.28,Na₂O/SiO₂(mol ratio)=0.035时,所得到的分子筛沿b轴方向生长最慢,产品形貌呈薄片状,厚度为130 nm;在一定范围内提高碱度,会使分子筛形貌逐渐变为纳米颗粒聚集体。ICP、NH₃-TPD和N₂吸附表征结果表明,所合成的分子筛SiO₂/Al₂O₃物质的量比、酸性质及孔道性质接近。催化反应评价结果表明,薄片状样品HZ-1由于在b轴方向上具有更短的扩散路径,且结晶度高,在催化甲醇转化反应中不仅表现出良好的选择性,双烯(乙烯+丙烯)收率可达60%以上;P/E比(丙烯/乙烯)最高可达8.4,在连续反应200 h后,甲醇转化率仍保持在95%以上,表现出优异的催化稳定性。     

Layer-by-layer assembly of zeolite crystals on glass with polyelectrolytes as ionic linkers

ZSM-5 crystals and glass plates tethered with trimethylpropylammonium iodide and sodium butyrate, respectively, (denoted as Z+, Z-, G+, and G-, respectively) were prepared. Treatment of G- with Z+ suspended in ethanol results in monolayer assembly of Z+ on G- (G-/Z+) with high surface coverage. The zeolite crystals have a strong tendency to closely pack and align with the b-axis normal to the glass plate, despite large positive zeta potentials. Subsequent treatment of G-/Z+ with Z- leads to second-layer assembly of Z- on G-/Z+ (G-/Z+/Z-), but with rather poor coverage. Sequential treatment of G+ with poly(sodium 4-styrenesulfonate)(Na+PSS-), poly(diallyldimethylammonium chloride) (PDDA+Cl-), and Na+PSS- followed by Z+ yields glass plates assembled with monolayers of Z+ with very high surface coverage through the composite polyelectrolyte linkers (G+/PSS-/PDDA+/PSS-/Z+). The zeolite crystals also have a strong tendency to closely pack and align with the b-axis perpendicular to the substrate plane. The binding strength between the zeolite crystals and glass plates is much higher in G+/PSS-/PDDA+/PSS-/Z+ than in G-/Z+. Repetition of the sequential PSS-/PDDA+/PSS-/Z+ layering for five cycles yields glass plates assembled with pentalayers of ZSM-5 crystals [G+/(PSS-/PDDA+/PSS-/Z+)(5)]. The observed degrees of coverage and alignment of zeolite crystals in each layer were very high up to the third layers despite the nonuniformity of the sizes and shapes of the zeolite crystals used in this study. This report thus demonstrates the feasibility of layer-by-layer assembly of micrometer-sized zeolite crystals on glass through electrostatic interaction between surface-bound, full-fledged ionic centers, especially by use of polyelectrolyes as the linkers.     

Aggregation-governed oriented growth of inorganic crystals at an organic template

X-ray studies performed during the growth of CdCO(3) and MnCO(3) crystals from supersaturated aqueous solutions, at fatty acid monolayer templates, reveal that the nucleates are nearly three-dimensional powders below a threshold supersaturation. However, at higher supersaturations, the crystals are preferentially oriented with the {0 1 2} direction vertical. Scanning electron microscope images of samples transferred to substrates show discrete crystals at low concentrations, while at higher concentrations the crystals self-aggregate to form linear chains and sheets. The authors speculate that preferential alignment at the organic-inorganic interface is enhanced as a consequence of oriented aggregation of crystals. The role of monolayer-ion interactions in governing the morphologies and the resulting orientation of the inorganic nucleate is discussed.     

Na2O-SiO2-Al2O3-NaCl-H2O体系中ANA和SOD沸石膜的水热合成

Na2O-SiO2-Al2O3-NaCl-H2O体系中，以水玻璃和准一水软铝石为原料，分别在 堇青石和玻璃载体上水热合成方沸石（ANA）和方钠石（SOD）沸石膜。研究水含量 、反应温度、反应时间与多次合成对膜结晶的影响。用XRD，SEM，EDX表征膜的晶 相、形貌和化学组成。堇青石负载方沸石膜在对95％（wt.)乙醇水溶液的渗透蒸发 实验中，水优先透过沸石膜的选择性显示了晶间孔的醇／水分离作用。非计量的 NaCl进入到在玻璃载体上成膜的方钠石笼中，致使该膜显示光致变色效应。     

Nanocomposite MFI-alumina membranes via pore-plugging synthesis: Genesis of the zeolite material

This paper presents a study of MFI-type zeolite crystal growth during hydrothermal synthesis of nanocomposite MFI-alumina membranes by the pore-plugging method, using the standard protocol described in a previous study [S. Miachon, E. Landrivon, M. Aouine, Y. Sun, I. Kumakiri, Y. Li, O. Pachtová Prokopová, N. Guilhaume, A. Giroir-Fendler, H. Mozzanega, J.-A. Dalmon, Nanocomposite MFI-alumina membranes via pore-plugging synthesis: specific transport and separation properties, J. Membr. Sci. 281 (2006) 228]. To this aim, the materials have been characterized by SEM, EDX, pure H2 gas permeance and n-butane/H2 mixture separation at different stages of the synthesis. The effect of synthesis time in the range of 4–89 h and the effect of a 9-h interruption after a 8-h hydrothermal synthesis have been surveyed, as well as the mean pore size and the alumina phase of the support inner layer. Our results suggest that an interruption during the synthesis is necessary to allow the zeolite precursor to diffuse into the support pores. This diffusion leads to a further growth of zeolite crystals into the support matrix without formation of a continuous zeolite film on top of the support, as is usually reported in the literature. The zeolite crystals are fully embedded into the support top layer after at least 53-h synthesis time, leading to high quality membranes in only one synthesis run. The nanocomposite MFI-alumina architecture at the nanoscale has important consequences in improving the gas separation performance of this kind of materials when compared to more conventional film-like structures. A method based on gas transport measurements has been used to determine the effective thickness of the separating material.     

Preparation and characterization of silicalite-1 membranes prepared by secondary growth of seeds with different crystal sizes

MFI-type zeolite particles of 0.1–1 μm in diameter were prepared by adjusting tetra-n-propylammonium hydroxide (TPAOH) and water contents in synthesis mixtures. Using those particles as seeds, MFI-type zeolite membranes were prepared on the surface of a porous mullite tube by secondary growth. The membranes were formed as polycrystalline zeolite layers on and inside the porous support, and the membranes were composed of the [h 0 h]-oriented crystallites. The membrane consisting of a-oriented crystallites could be also prepared. However, the a-oriented zeolite layers were not active on the permeation properties of butanes. Rather the size and loaded amount of the seed particles influenced on the permeation properties through the membranes. As a result, the n-C₄H₁₀/i-C₄H₁₀ permselectivity could be increased to 220 by adjusting the size and the loaded amount of particles. These results suggest that the number of loaded particles affects on the permeation properties through the membranes.     

Unprecedented reversible redox process in the ZnMFI-H2 system involving formation of stable atomic Zn(0)

In its element: Zn(2+) at the M7 site of MFI-type zeolites activates H(2), via ZnH and OH species, and leads to Zn(0) species. The Zn(0) species returns to its original state, a Zn(2+) ion, upon evacuation of the zeolite at 873?K (see picture). The formation of the Zn(0) species is supported by DFT calculations.