高硅ZSM-5分子筛和二次合成Ti-ZSM-5分子筛的结构

运用度角旋转（MAS）和交叉极化（CP）等核磁共振波谱和红外光谱技术，分别对采用不同模板剂制备的高硅ZSM－5分子筛和以此为母体，经气固同晶取代法得到Ti－ZSM－5分子筛的结构特性进行了研究．结果表明：在水热法合成高硅ZSM-5分子筛过程中，模板剂明显制约着所制得的分子筛的结构特性．通过选用合适的模板剂，可直接获得具有正交晶系结构的高硅ZSM－5分子筛．在随后的气固相同晶取代过程中，钛原子通过占据分子筛骨架中的缺陷位进入骨架，形成具有一定Ti／Si比例的钛硅分子筛（Ti－ZSM－5）。骨架结构中缺陷位的含量直接影响分子筛的载钛量。     

不同硅铝比的Cu-ZSM-5/堇青石整体式催化剂的NO分解反应性能

 考察了原位合成的不同硅铝比的Cu－ZSM－5／堇青石整体式催化剂上的NO分解反应．结果表明,在573～773K的温度范围内,硅铝比分别为60,55和40的催化剂在723K下NO的转化率最高,而硅铝比小于25的催化剂上的NO转化率很低．低温有利于N2O的生成．整体式催化剂上的NO转化率低于单纯的分子筛催化剂Cu－ZSM－5,但其催化转换频率高于后者．     

Ti-ZSM-11的红外光谱研究

随着杂原子分子筛研究领域的开拓与发展，近年来，对钛硅沸石的研究逐渐增多．Ti－ZSM－11（TS－2）型分子筛是由Reddy，Ratanasarny等[1]首先合成的．钛硅沸石的表征与其它杂原子分子筛相比较为复杂，对杂原子Ti是否进入了骨架还没有一个直接的证据，且争议较多．在红外光谱的研究中，对960cm－1－980cm－1区间的特征吸收的归属也存在着很大的分歧[2－4]．钛硅沸石在H2O2对有机化合物的选择氧化领域有极其优良的催化性能[1]，因此，对它的开发有广泛的应用前景．本文以动态和静态相结合的水热晶化法合成了Ti－ZSM－11型分子筛．IR光…     

静态水热晶化法高效合成MCM-22分子筛

 采用静态水热晶化法，在Na2O－Al2O3－SiO2－HMI－H2O（HMI：六亚甲基亚胺）体系中，在HMI／SiO2摩尔比为0．09，H2O／SiO2摩尔比为12，晶化时间为60～80h的条件下，合成了MCM－22分子筛．利用固体硅胶表面的吸附性能提高模板剂的局部浓度，从而实现了分子筛的高效合成．对合成条件的研究结果表明，以比表面积（486m2／g）大、反应性能好的硅胶为硅源是静态水热晶化法高效合成MCM－22分子筛的关键，而成胶老化方式对MCM－22分子筛的晶化影响不大．产物的晶相和转晶的类型取决于合成凝胶的初始硅铝比．当SiO2／Al2O3摩尔比＝18～80时可以合成出MCM－22，当SiO2／Al2O3＝13～17时可以合成出MCM－49．硅铝比较低（如SiO2／Al2O3＝20）时，MCM－22分子筛易转晶为MOR分子筛，而在硅铝比较高（如SiO2／Al2O3＝50）时，可转晶为ZSM－5分子筛．     

光离子检测气相色谱法分离分析氨及其氧化产物

本文采用光离子化和热导池两个检测器串联,以5A钙型分子筛填充柱与Chromesorb 104+2％KOH填充柱并联方式,成功地定量分离分析了N2,O2,NO或NO_2,N_2O和NH_3的混合气体。     

DeNOx催化剂FeZSM－5／RaneyFe的制备

 用原位晶化法合成了FeZSM－5／RFe（RFeRaneyFe）催化剂．合成液的组成为5Na2O·100SiO2·10TPABr·7000H2O，pH＞11．5．合成液中不含Al，ZSM－5分子筛的骨架Al只来源于RaneyFe的表面．此法提高了ZSM－5分子筛中骨架Al的稳定性和分子筛上Fe离子的负载量．FeZSM－5／RFe用作DeNOx催化剂时具有较高的活性和水热稳定性．     

高硅分子筛ZSM-22的动态合成及表征

 以1，6－己二胺（DAH）为模板剂，采用水热条件下的动态合成方法，合成出结晶度良好的ZSM－22晶体．研究表明，合成的关键是避免ZSM－5分子筛的生长，当n（Si）／n（Al）＝25～65，n（H2O）／n（SiO2）＝16．3～40．3，n（DAH）／n（Si）＝0．1～0．6和T＝428～448K时，都能稳定合成出ZSM－22分子筛．采用TEM，XRD，TG－DTA和NH3－TPD等方法，对ZSM－22晶体的形貌，生长动力学，模板剂的作用以及硅铝比对分子筛酸性的影响等进行了较详细的研究．实验结果和理论计算证实，1，6－己二胺分子以首尾相连的方式，线性排列并完全充满ZSM－22的十元环孔道，同时起到结构导向和骨架电荷平衡的作用．     

晶化时间对ZSM-5分子筛物化性质及催化性能的影响

 考察了ZSM－5分子筛在晶化过程中的变化规律及其在苯与乙烯气相烷基化制乙苯反应中的催化性能．结果表明,当晶化时间为70h时,分子筛晶体开始出现;晶化90h时无定形物相基本消失．晶化时间从90h再延长至150h,ZSM－5分子筛晶粒的大小、形貌和体相硅铝比都基本不变,但分子筛表面的硅铝比逐渐降低．以晶化时间为90h的ZSM－5分子筛原粉为活性组元制备的催化剂,对苯与乙烯气相烷基化制乙苯反应表现出最佳的催化性能．     

以环己胺为模板剂的ZSM－35分子筛的合成及其催化性能

 采用环己胺为有机模板剂成功地合成出ZSM－35分子筛．反应釜的转速对ZSM－35的晶化过程有明显的影响．NH3－TPD结果显示ZSM－35的酸性分布与ZSM－5分子筛类似，但ZSM－35具有强于ZSM－5的酸性中心．酸碱浸泡试验及热分析结果表明ZSM－35具有良好的耐酸碱性和热稳定性．在连续流动的固定床反应装置上，将担载少量镍的ZSM－35分子筛催化剂用于催化裂化汽油的加氢异构化反应，结果表明，Ni／ZSM－35催化剂可降低汽油中的烯烃含量，增加异构烷烃和芳烃的含量，从而提高汽油的质量．     

ZSM－5（核）／AlPO4－5（壳）双结构分子筛的合成与催化裂化性能

 采用X射线衍射、扫描电镜、X射线能量散射谱、红外光谱和核磁共振等多种物化方法对合成的ZSM－5（核）／AlPO4－5（壳）双结构分子筛进行了表征，证明这种材料具有以ZSM－5为核层、以AlPO4－5为壳层的双结构特征．考察了合成条件对ZSM－5（核）／AlPO4－5（壳）分子筛形貌的影响，发现ZSM－5分子筛的加入方式对产物的形貌有较大影响．重油裂化反应结果表明，ZSM－5（核）／AlPO4－5（壳）双结构分子筛的催化性能比ZSM－5和ZSM－5／AlPO4－5机械混合分子筛样品好，表现为原油转化率和低碳烯烃、汽油及柴油收率提高．     

钛硅分子筛中铝杂质对其性能的影响

 以四丙基溴化铵为模板剂,以硅溶胶为硅源,采用水热合成法制备了不同铝杂质含量的钛硅分子筛,并系统考察了铝杂质对钛硅分子筛性能的影响．结果表明,原料中的铝杂质可促进钛硅分子筛晶化,但同时也引入了酸性中心;在丙烯环氧化反应中,铝杂质形成的酸性中心会催化环氧丙烷与溶剂的副反应;加入少量碱性添加物可抑制铝杂质的酸催化作用,提高环氧丙烷的选择性,但过量碱性添加物会使钛硅分子筛失活．     

Equilibrium and kinetic analysis of CO2-N2 adsorption separation by concentration pulse chromatography

CO2 and N(2) adsorption kinetics and equilibrium behaviours have been studied with silicalite, NaY and 13X by using concentration pulse chromatography for the separation of these gases in the present study. Adsorption Henry's Law constants, the heat of adsorption values, micropore diffusion coefficients and corresponding activation energies are determined experimentally and the three different mass transfer mechanisms are discussed. From the equilibrium data, the corresponding separation factors are obtained for the adsorption separation processes. The heat of adsorption values as well as the Henry's Law adsorption equilibrium constants of CO(2) are much higher than those of N(2) for all the adsorbents studied. 13X, NaY and silicalite all have good separation factors for CO(2)/N(2) system based on equilibrium processes. The order of the equilibrium separation factors is 13X (Ceca)>13X (Zeochem)>NaY (UOP)>silicalite (UOP). Equilibrium selectivity favours CO(2) over N(2). Micropore diffusion resistance is the definite dominant mass transfer mechanism for CO(2) with silicalite and NaY.     

Synthesis of submicron polycrystalline MFI zeolite films on porous ceramic supports

This paper reports preparation and properties of ultra-thin MFI-type zeolite (silicalite) films on sol–gel derived mesoporous 8 mol% yttria doped zirconia (YZ) supports by the in situ synthesis method. Only non-continuous zeolite films were obtained on the as-synthesized YZ supports (calcined at 450°C). Continuous polycrystalline pure silicalite films, with a thickness of 0.5–0.7 μm, could be grown on the YZ supports pretreated at 700°C. The difference in the oxygen vacancy defect concentrations in these two types of YZ supports is suggested to explain the different results of growing silicalite films. Moreover, defect free 2–3 μm thick silicalite films were also prepared on the α-alumina supports under the same synthesis conditions. The silicalite layer on the YZ support offers a significantly lower mass transfer resistance as compared to that on the alumina support. Single gas permeation data of hydrogen, methane and ethane through these membranes were measured and compared with those of silicalite membranes prepared by other groups. The alumina supported silicalite membranes prepared in this work show better separation factors than the literature values. The zeolite film on the YZ support is less resistant to the stress induced in the step of template removal as compared to the zeolite film on the alumina support.     

Molecular simulation of adsorption and diffusion of chlorinated alkenes in ZSM-5 zeolites

In this work, adsorption and diffusion of trichloroethylene (TCE) and tetrachloroethylene (PCE) in ZSM-5-type zeolites were studied using molecular simulation methods. Grand canonical Monte Carlo technique was to calculate adsorption isotherms and heats of vaporization of TCE and PCE in zeolite. The results demonstrated that the Pnma-P2(1)2(1)2(1) symmetry transition of the zeolite framework has no significant effect on the TCE adsorption capacity of the silicalite, but it causes an increase of the PCE adsorption capacity. Simulations using a silicalite framework with Pnma symmetry showed that the adsorption capacity of the silicalite was limited to five molecules per unit cell. However, when a framework with P2(1)2(1)2(1) symmetry was used in the simulations, the capacity reached to eight molecules per unit cell, which is the actual adsorption capacity. To calculate intracrystalline diffusion coefficients of these compounds, molecular dynamics simulations were performed at different temperatures and loadings. The results show that the zeolite symmetry has a significant impact on diffusion coefficients of the sorbate molecules.     

Elaboration of Urease Adsorption on Silicalite for Biosensor Creation

A possibility of efficient urease adsorption on silicalite for the purpose of biosensor creation was investigated. The procedure of urease adsorption on silicalite is notable for such advantages as simple and fast performance and non‐use of toxic or auxiliary compounds. Optimal conditions for modifying transducer surfaces with silicalite and subsequent urease adsorption on these surfaces were selected. The working parameters of the created biosensor were optimized. The developed biosensor with adsorbed urease was characterized by good intra‐reproducibility (RSD – 4.5 %), improved inter‐reproducibility (RSD of urea determination is 9 %) and operational stability (less than 10 % loss of activity after 10 days). Besides, the developed method for enzyme adsorption on silicalite was compared with the traditional methods of urease immobilization in biosensorics. Working conditions of the produced biosensor (pH and ionic strength) were shown to be close to those of the biosensor based on urease immobilized in GA vapor. For these reasons, it was concluded that the method of enzyme adsorption on silicalite is well‐suited for biosensor standardization aimed at its further manufacture.     

Zeolite synthesis from tetraalkylammonium silicate gels

Siliceous zeolite synthesis gels containing tetraalkylammonium (TAA⁺) and sodium cations were studied using X-ray diffraction, elemental analysis, ion exchange, ²⁹Si magic-angle spinning nuclear magnetic resonance spectroscopy, and scanning electron microscopy. The TAA⁺ cations are encapsulated in silicate cages, and silicalite is formed via the rearrangement of these cages by the breaking and reformation of siloxane bonds. Tetrabutylammonium (TBA⁺) cations promote silicalite growth, but not as effectively as tetrapropylammonium (TPA⁺) because the larger TBA⁺ cations do not conform as well to the silicalite lattice, thus forming an intergrowth of the silicalite-1 and silicalite-2 structures. The time to nucleate silicalite is not affected by the TBA⁺ content of the gel, but the rate of silicalite crystal growth increases with increasing TBA⁺ in the gel. The TBA⁺ occupies all the channel intersections of the silicalite formed. Tetraethylammonium (TEA⁺) cations are encapsulated in silicate cages, but not to the same extent as TPA⁺ and TBA⁺, because TEA⁺ is not as hydrophobic. No silicalite forms in the TEA⁺ silicate gel. The addition of tripropylamine (TriPA) to a TPA⁺ silicate gel has no effect on the kinetics of silicalite formation. TriPA does not incorporate into the gel because it is neutral and, therefore, does not experience a coulombic attraction to the negatively charged surface of the gel.     

Ti－Si沸石表面吸附物种的TPSR－TPD研究

氯丙烯在不同催化剂表面上吸附的ＴＰＤ结果表明：在ＴＳ－１上有三重脱附峰，而在ＴｉＯ２／Ｓｉｌｉｃａｌｉｔｅ上仅有单峰。Ｈ_２Ｏ_２或分子Ｏ_２在催化剂表面吸附后，在脱附物种中可用质谱检测到原子Ｏ（１６）物种；说明Ｈ_Ｏ_２或分子Ｏ_２在样品表面存在解离吸附；并发现解离分子Ｏ_２的活性很低。ＴＳ－１能同时吸附氯丙烯和Ｈ_２Ｏ_２，而在ＳｉＯ_２／Ｓｉｌｉｃａｌｉｔｅ表面的吸附却与吸附顺序有关。环氧化活性顺序如下：ＴＳ－１（ＴＰＡＯＨ）＞ＴＳ－１（ＴＰＡＢｒ＋ＮａＯＨ）＞ＴｉＯ_２／Ｓｉｌｉｃａｌｉｔｅ。ＴＳ－１沸石的高氧化活性可能与Ｈ_２Ｏ_２吸附后表面原子Ｏ（１６）的形成有关。     

Effect of structural analogy between ZSM-5 and silicalite catalysts on the oxidative methylation of toluene with methane

Summary With ZSM-5 and silicalite (both initial and BaO modified) the yield of styrene, the most desirable reaction product, was highly represented when BaO modified silicalite was used as catalyst for the reaction. The catalytic results fitted the basicity, surface area and structural crystallinity.     

重量法测定环戊烷在silicalite-1分子筛上的吸附特性

用智能重量分析技术 (IGA)研究了环戊烷在silicalite 1分子筛上的吸附特性。结果表明 ,随着温度的降低 ,环戊烷的吸附等温线从第一类型过渡为第四类型 ,在 2 5 4K和 2 74K温度下吸附等温线呈现滞后环 ,为第四类型 ,而吸附等温线在 30 4K、32 3K下为阶梯形 ,在 35 4K、42 3K温度下呈第一类型 ,其中 42 3K温度下的吸附等温线可准确的用Langmuir方程来描述。本文同时讨论了吸附质分子间以及吸附质和吸附剂间的相互作用、分子结构特性、分子筛对吸附质分子的空间位阻、分子筛的能量不均匀表面等对环戊烷在silicalite 1分子筛上吸附性能的影响     

Separation of acetic acid-water mixtures by pervaporation through silicalite membrane

Polycrystalline silicalite membranes were prepared on two kinds of porous supports by hydrothermal synthesis. The pervaporation performance of the silicalite membrane obtained was investigated using an acetic acid-water mixture as a feed. The silicalite membrane on the sintered stainless steel support selectively permeates acetic acid in the concentration of the feed acetic acid in the region of 5 to 40 vol%. However, the membrane on the porous alumina support showed no separation for the aqueous acetic acid solution. From the fact that the top layer of the membrane on the alumina support was not composed of pure silicalite but ZSM-5 zeolite crystals, which contained Brønsted acidic sites (Si(OH)Al) in the framework, it was suggested that the acidic sites associated with the framework aluminums play an important role in the separation of the acetic acid-water mixture. A long-term test of the pervaporation was also carried out to clarify the stability of the membrane.