HY沸石超笼“半三明治”环戊二烯铁物种的接枝

在真空条件下研究了Cp₂Fe在HY沸石表面的接枝反应，并用原位FTIR、ICP、XRD、TPD-MS和UV-Vis DRS等方法对接枝产物的组成、结构及性质进行了表征。结果表明，在低于423 K的温度下，Cp₂Fe可以强吸附在沸石的超笼内，并被氧化为Cp₂Fe⁺阳离子；当在423 K长时间加热时，Cp₂Fe⁺可与超笼表面的酸性中心发生化学反应，脱除一个环戊二烯基团，在沸石超笼形成“半三明治”环戊二烯铁CpHFe(OZ≡)₃(Z为沸石骨架Si或Al原子)表面物种。一个超笼中可接枝3个CpHFe基团，该物种在真空、惰性气体气氛和473 K以下能够在表面稳定存在。接枝反应不破坏HY的骨架结构，修饰后HY沸石的BET比表面积和微孔体积大约降低一半。     

表面富锡MCM-41分子筛的表面金属有机化学制备及其对苯酚羟基化催化反应性能研究

采用SnBu₄在MCM-41表面的接枝反应和后续处理制备出了一种只在表面含锡的MCM-41型介孔分子筛。通过与采用纳米SnO₂和MCM-41机械混合法、SnCl₄浸渍法、水热合成法等制备的具有相当硅锡比(Si/Sn≈100)的SnMCM-41分子筛进行结构和对苯酚羟基化反应催化性能的比较发现， 由该法所得分子筛的水热稳定性明显提高，并在苯酚羟基化反应中表现出优良的催化活性、选择性和过氧化氢利用率。本文还详细考察了该催化剂对苯酚羟基化反应的最佳反应条件。     

SnMe3/Pt/HY分子筛的合成与表征

在高真空系统下研究了SnMe4与Pt修饰的HY沸石分子筛表面的接枝反应,并用元素分析、FT-IR,XRD,DRS,BET,GC等表征了接枝产物的组成和性质。结果表明：Pt／HY沸石的表面羟基可以与SnMe4在常温下反应,将三甲基锡基团接枝在沸石的超笼中。Pt／HY与SnMe4发生接枝反应后晶相结构没有改变,微孔体积和BET表面积都下降。     

CuCl2和HY分子筛的表面反应及Cu/Y分子筛的制备及其催化甲醇氧化羰基化

以CuCl₂为前驱物与HY分子筛进行固相离子交换制备了Cu/Y催化剂,采用热重方法研究了CuCl₂与HY分子筛的表面固相离子交换反应,结合活性测试表明催化剂中高度分散的CuCl和离子交换形式的Cu⁺物种是甲醇氧化羰基化合成碳酸二甲酯的催化活性中心。X射线光电子能谱表征和元素分析结果表明,活性金属Cu主要以CuCl形式存在于分子筛外表面,而在分子筛笼内则以交换的Cu⁺和少量吸附的CuCl形式存在。与以CuCl为交换铜源所制催化剂相比,以CuCl₂为铜源制备的催化剂Cu含量低,催化活性更高。     

四甲基锡在MCM-41分子筛表面的接枝反应及产物性能

研究了真空条件下SnMe4在MCM-41分子筛表面的接枝反应，并用元素分析、ICP、GC-MS、XRD、FTIR、DRS、13C及119Sn MAS NMR、XPS、BET、TPD、TPR等方法对产物的组成、结构和性质进行了表征.结果表明, 两者可以定量地进行化学反应，将确定数目的甲基锡基团接枝在分子筛表面, 形成SnMe3/MCM-41物种；接枝反应发生在分子筛表面上, 不破坏MCM-41分子筛骨架结构；改性分子筛的BET比表面积有所降低，孔体积变小, 表面性质发生变化.四甲基锡在MCM-41上接枝反应的温度为343 K,比它与HY沸石的反应温度(193 K)高得多，并且产物SnMe3/MCM-41的热稳定性也高于SnMe3/HY.     

介孔分子筛表面丁基锡的制备和性能

在高真空系统中研究了MCM-41介孔分子筛与四丁基锡的反应,并用元素分析、气体容量分析、XRD、FTIR、 ¹³C及 ¹¹⁹Sn MAS NMR和氮气及烃吸附等方法表征了产物的组成、结构和性质。结果表明,MCM-41的表面羟基与四丁基锡能在150℃发生反应,在200℃预脱水处理后的MCM-41上生成组成为(≡Si-O) _xSn(n-Bu) _4-x的表面混合物,而在500℃预脱水处理后的MCM-41上则得到组成为≡Si-O-Sn(n-Bu)₃的表面单接枝物种;表面接枝丁基锡物种导致MCM-41的孔道尺寸变小,表面组成改变,从而引起对烷烃的吸附行为发生变化。     

一种合成高水热稳定性微孔-介孔复合分子筛β沸石/MCM-41的新方法

首次以β沸石作为硅铝源制备了β沸石/MCM-41微孔-介孔复合分子筛材料，通过XRD、IR、N₂吸附脱附、SEM和水热处理等手段对复合材料进行了表征，并与MCM-41和β沸石及二者的机械混合物的有关性能进行了对比研究。结果表明，复合分子筛明显不同于机械混合物，其水热稳定性远远高于普通方法合成的介孔分子筛，而且发现通过改变体系的n_Na/n_Si比，可以调变复合样品中的微孔、介孔相的相对含量。     

CuY制备方法对其催化甲醇氧化羰基化活性中心的影响

以Cu(NO₃)₂为铜源,以NaY和HY分子筛为载体,通过溶液离子交换法和等体积浸渍法制备了不同的无氯CuY催化剂,并进行了气相甲醇氧化羰基化催化活性研究。通过浸渍法制备的催化剂Cu含量为10%,而以NaY和铜氨溶液离子交换制备的催化剂Cu含量只有6.3%,但其催化活性和选择性均较好。通过催化剂的Cu元素分析、低温氮吸附-脱附、XRD、H₂-TPR、XPS和TPD等表征表明,溶液离子交换法制备的催化剂,Cu物种以离子的形式高度分散于分子筛骨架结构中,较好地保持了分子筛晶体结构,并对甲醇有较强的吸附能力,催化活性较高,而将等体积浸渍Cu(NO₃)₂溶液后的HY或NaY分子筛,在400 ℃焙烧过程中,发生了固体离子交换反应,形成了连接于分子筛骨架的Cu²⁺,但以HY为载体更容易进行固体离子交换,未交换的铜物种以CuO的形式分散到分子筛表面。在600 ℃高温活化中,催化剂中Cu²⁺可部分还原为活性物质Cu⁺,但以NaY和铜氨溶液离子交换制备的催化剂Cu²⁺自还原能力最大。     

C2-C2直链烯烃在HY 和H-ZSM-5分子筛上的吸附

采用ONIOM(B3LYP/6-311++G(d,p):UFF)分层计算方法, 研究了C₂-C₅直链烯烃在HY 和H-ZSM-5 分 子筛上的吸附性质. 理论计算结果表明: 烯烃与分子筛的Br?nsted 酸性位相互作用形成π配位超分子复合物; 随着碳链的增长, 烯烃的吸附能增加, 增加量近似为一个常数(HY 分子筛: 约12 kJ·mol^-1; H-ZSM-5 分子筛: 约 25 kJ·mol^-1), 与烷烃在分子筛上的吸附具有相同的规律. 双键位置对烯烃的吸附能影响很大, 2位烯烃的吸附能 要远大于1 位烯烃的吸附能. 不同类型分子筛对烯烃的吸附性能也有很大差别, 由于局域效应的影响, 小孔径 H-ZSM-5分子筛上的吸附能大于大孔径的HY分子筛,而且碳链越长,这种差别越大.从微观结构上看,吸附的烯 烃与H-ZSM-5分子筛酸性位的距离要远大于它们与HY分子筛酸性位的距离, 这是由于不同类型分子筛的微孔 结构产生的范德华作用是不同的,这种作用随着孔径的减小而增强.前线轨道分析表明, 对于小分子烯烃,大孔径 HY分子筛对其催化活性相近,而小孔径H-ZSM-5分子筛随着烯烃碳原子数的增加催化活性有减弱的趋势.     

高硅 Na-ZSM-5 分子筛表面 NO 的常温吸附-氧化机理

 采用程序升温表面反应 (TPSR) 和原位漫反射红外光谱 (DRIFTS) 等手段研究了常温下 NO 和 O₂ 在高硅 Na-ZSM-5 分子筛上吸附-氧化反应机理. 结果表明, Na-ZSM-5 分子筛上 NO 的催化氧化过程中伴随着显著的 NO₂ 物理吸附, 表现为 NO 氧化和 NO₂ 吸附间的动态平衡. Na-ZSM-5 分子筛表面 NO_x 吸附物种的 TPSR 和原位 DRIFTS 表征表明, 化学吸附的 NO 和气相中的 O₂  在 Na-ZSM-5 表面反应生成吸附态的 NO₃, 并继续与 NO 作用生成弱吸附的 NO₂  和 N₂ O₄, 它们吸附饱和后释放出来; 其中, 强吸附的 NO₃ 在 NO 氧化过程中起到了反应中间体的作用, 同时也促进了 NO 的吸附.     

HY Zeolite Modified by Liquid Silane Deposition and Its Catalytic Activity in Selective tert-Butylation of Naphthalene

HY zeolites were modified by chemical liquid deposition with i-C₄H₉Si(OC₂H₅)₃, followed by hydrothermal treatment. The samples were characterized by X-ray diffraction, N₂ adsorption and pulse mass analysis to investigate the influence on framework structure, specific surface area, pore diameter and adsorption behaviors. The catalytic performances of HY zeolite and the modified samples in the alkylation of naphthalene with tert-butyl alcohol were also evaluated. The results showed the modification of HY zeolite did not change framework structure but increased specific surface area, decreased average pore diameter, and reduced the size of pore opening. Catalytic activity of the modified HY zeolite catalyst for tert-butylation of naphthalene was decreased compared with that of HY zeolite catalyst while shape-selectivity of 2,6-di-tert-butylnaphthalene (2,6-DTBN) was increased obviously, the highest 2,6-DTBN/2,7-DTBN ratio of 6.62 obtained.     

镧改性的CuHY分子筛中铜离子的分布及其对吸附脱硫性能的影响

在氮气气氛下采用等体积浸渍法制备了载Cu的HY和LaHY分子筛.用x射线衍射(XRD)、N2吸附、氨程序升温脱附和X射线光电子能谱对分子筛进行了表征.通过多晶XRD确定了Cu2+离子在Y型分子筛笼内的结构与分布,并测定了分子筛在含二苯并噻吩(DBT)的模拟柴油中的吸附脱硫性能.结果表明,前驱体CuCl2中的大部分Cu物种与HY和LaHY分子筛进行了离子交换.对于La3+改性的CuHY分子筛(CuLaHY),进入分子筛超笼中的Cu2+离子与骨架氧和水分子配位,牢固地定位于Y型分子筛超笼的SⅡ及SⅢ位;对于CuHY分子筛,超笼中的Cu2+离子只接近于SⅡ及SⅢ位.极少部分CuCl分子高度分散在分子筛笼内,没有定位.处于超笼中SⅡ及SⅢ位的Cu2+离子对模拟柴油中的DBT分子具有吸附作用,是吸附脱硫的活性中心.CuLaHY分子筛的吸附脱硫性能优于CuHY分子筛.当模拟柴油中含有萘时,萘与DBT分子会产生竞争吸附.     

甲基噻吩在HY分子筛上的吸附、脱附及转化行为

由NH₄Y分子筛制备了HY分子筛,运用N₂吸附、NH₃-TPD和Py-FTIR等手段表征HY分子筛的物化性能;采用智能重量分析仪(IGA)方法研究了甲基噻吩(2-甲基噻吩、3-甲基噻吩)在HY分子筛上的吸附-脱附行为;采用程序升温脱附-质谱(TPD-MS)联用手段研究了甲基噻吩在HY分子筛上的转化行为。结果表明,在200 ℃下 2-甲基噻吩和3-甲基噻吩在HY分子筛中的强B酸上发生强化学吸附作用,与B酸结合后生成了甲基噻吩的碳正离子结构进而发生了歧化反应、脱烷基反应以及裂化反应;与2-甲基噻吩不同的是,3-甲基噻吩与HY通过一定的氢转移反应生成了3-甲基四氢噻吩,且200 ℃吸附条件下3-甲基噻吩比2-甲基噻吩更容易发生裂化反应。     

Reactivities of tetraalkyltin complexes toward Pt/HY zeolite

Tetraalkyltin complexes, SnR₄ (R = Me, Et, Pr, Bu) could react with Pt/HY at 193, 243, 273 and 333 K, respectively. The reactions occurred on the surface of the zeolite and the organotin grafted zeolites were characterized in detail. The framework and the microporous structure of the grafted Pt/HY zeolites were retained. However, the modified zeolites showed better size selectivity in the absorption of hydrocarbons.     

The kinetics of ethanol adsorption from the aqueous phase onto zeolite NaZSM-5

The kinetics of the isothermal adsorption of ethanol from an aqueous solution onto a hydrophobic zeolite of the NaZSM-5 type in the temperature range 298–333 K was investigated. Specific shape parameters of the adsorption degree curves were determined. The changes in the specific shape parameters of the adsorption degree curves with temperature were determined. The kinetic parameters of ethanol adsorption (E_a,ln A) were determined by the initial rate, the saturation rate and the maximum rate methods as well as from the Johnson, Mehl and Avramy equation. The kinetic model of ethanol adsorption kt=[1−(1−α)^1/3] was determined by the “model fitting” method. Ethanol adsorption from aqueous solution onto NaZSM-5 is a kinetically controlled process limited by the rate of three-dimensional movement of the boundary layer of the adsorption phase. A model for the mechanism of ethanol adsorption onto NaZSM-5 is suggested on the basis of the kinetic model. Ethanol molecules in aqueous solution are associated in clusters. The activation energy of the adsorption process corresponds to the energy required for the detachment of an ethanol molecule from a cluster and its adsorption onto the zeolite.     

Hydrocarbon radicals and nitroxy complexes on the surface of HZSM-5 and CuZSM-5 zeolites: An ESR study

The conditions favorable for the formation of oligomer and benzene cation radicals upon C₂H₄, C₆H₆, and C₃H₆ adsorption on thermally activated HZSM-5 and CuZSM-5 zeolites were studied. In the case of isolated copper ions, the radicals were shown to be formed from C₃H₆ but not from C₂H₄ and C₆H₆. Paramagnetic nitroxy complexes, which were formed as a result of the interaction of adsorbed hydrocarbons C₂H₄, C₆H₆, and C₃H₆ with NO and NO₂, were revealed on HZSM-5 zeolite and Al₂O₃. Hydrocarbon radicals and nitroxy complexes are localized on different zeolite sites. Nitroxy complexes are formed on aluminum cations. The role of radicals and nitroxy complexes in the process of NO _x selective catalytic reduction by hydrocarbons on the zeolites was discussed on the basis of the temperature dependences of the concentrations of these species.     

Construction of macromolecular model and analysis of oxygen absorption characteristics of Hongyang No. 2 coal mine

Understanding the molecular structure characteristics of coal from the molecular level is of great significance for realizing rational utilization and efficient transformation of coal. The molecular structure of coal samples from 1304 working face in No.13 coal seam of Hongyang No.2 Mine (HY) was studied by industrial analysis, elemental analysis, Nuclear magnetic resonance carbon spectroscopy (¹³C NMR) and Fourier transform infrared spectroscopy (FTIR). The results show that the aromatic compounds in coal samples of HY are mainly naphthalene ring structures. The aliphatic structure mainly consists of methyl, ethyl side chains and cycloalkanes. The ratio of aromatic bridge carbon to weekly carbon in molecular structure is 0.17. Oxygen atoms exist in the form of carbonyl, hydroxyl, and ether bonds, nitrogen atoms exist in the form of pyridine and pyrrole respectively, and sulfur atoms exist in the form of thiophene. Based on this, the planar structure model of coal macromolecule in HY is constructed, and its molecular formula is C₁₂₉H₈₈O₂₉N₂S, and its molecular weight is 2160. The structure optimization and annealing kinetics simulation of a single macromolecule model were carried out, and a stable three-dimensional coal model of HY was obtained. In addition, the oxygen absorption characteristics of coal samples in HY were studied by molecular dynamics and quantum chemistry. The results show that the adsorption capacity of the Wiser model is less than that of HY coal model. This is because, compared with the Wiser model, the content of oxygenated aliphatic hydrocarbons in the molecular structure of HY coal is higher, and the condensation degree of polycyclic aromatic hydrocarbons is lower. Due to the stronger physical adsorption capacity of hydroxyl, ether bond, and carbonyl on O₂, HY Mine has stronger physical adsorption capacity on O_2.     

Catalytic cracking of C5+ gasoline over hy zeolite

The catalytic conversion of a C5+ natural gasoline over the HY zeolite has been studied. The results show the formation of C2, C3 and C4 hydrocarbons with an apparent activation energy of ca. 39 kJ mol^-1. This revised version was published online in June 2006 with corrections to the Cover Date.     

Selective methane chlorination to methyl chloride by zeolite Y-based catalysts

The CH₄ chlorination over Y zeolites was investigated to produce CH₃Cl in a high yield. Three different catalytic systems based on Y zeolite were tested for enhancement of CH₄ conversion and CH₃Cl selectivity: (i) HY zeolites in H⁺-form having various Si/Al ratios, (ii) Pt/HY zeolites supporting Pt metal nanoparticles, (iii) Pt/NaY zeolites in Na⁺-form supporting Pt metal nanoparticles. The reaction was carried out using the gas mixture of CH₄ and Cl₂ with the respective flow rates of 15 and 10 mL min⁻¹ at 300–350 °C using a fixed-bed reactor under a continuous gas flow condition (gas hourly space velocity = 3000 mL g⁻¹ h⁻¹). Above the reaction temperature of 300 °C, the CH₄ chlorination is spontaneous even in the absence of catalyst, achieving 23.6% of CH₄ conversion with 73.4% of CH₃Cl selectivity. Under sufficient supplement of thermal energy, Cl₂ molecules can be dissociated to two chlorine radicals, which triggered the C-H bond activation of CH₄ molecule and thereby various chlorinated methane products (i.e., CH₃Cl, CH₂Cl₂, CHCl₃, CCl₄) could be produced. When the catalysts were used under the same reaction condition, enhancement in the CH₄ conversion was observed. The Pt-free HY zeolite series with varied Si/Al ratios gave around 27% of CH₄ conversion, but there was a slight decrease in CH₃Cl selectivity with about 64%. Despite the difference in acidity of HY zeolites having different Si/Al ratios, no prominent effect of the Si/Al ratios on the catalytic performance was observed. This suggests that the catalytic contribution of HY zeolites under the present reaction condition is not strong enough to overcome the spontaneous CH₄ chlorination. When the Pt/HY zeolite catalysts were used, the CH₄ conversion reached further up to 30% but the CH₃Cl selectivity decreased to 60%. Such an enhancement of CH₄ conversion could be attributed to the strong catalytic activity of HY and Pt/HY zeolite catalysts. However, both catalysts induced the radical cleavage of Cl₂ more favorably, which ultimately decreased the CH₃Cl selectivity. Such trade-off relationship between CH₄ conversion and CH₃Cl selectivity can be slightly broken by using Pt/NaY zeolite catalyst that is known to possess Frustrated Lewis Pairs (FLP) that are very useful for ionic cleavage of H₂ to H⁺ and H⁻. Similarly, in the present work, Pt/NaY(FLP) catalysts enhanced the CH₄ conversion while keeping the CH₃Cl selectivity as compared to the Pt/HY zeolite catalysts.     

Base-induced Brönsted Acid Sites on Dealuminated HY Zeolite: A Solid-state NMR Spectroscopy Study

Using trimethylphosphine (TMP) and d₅-pyridine(deuterated pyridine) as the basic probe molecules, the concentrations of Brönsted acid sites on both HY zeolite and dealuminated HY zeolite have been quantitatively determined using solid-state ¹H and ³¹P magic-angle spinning (MAS) NMR. After adsorption of the probe molecules, the concentration of Brönsted acid sites on the dealuminated HY zeolite increases by about 25%, whereas that in the parent HY sample remains almost unchanged. The increase in the concentration of Brönsted acid sites is due to the appearance of base-induced Brönsted acid sites in the dealuminated HY zeolite. The terminal SiOH in the vicinity of the aluminum atom is “induced” to form a bridging hydroxyl group (SiOHAl) in the presence of the basic probe molecules. The mechanism of formation of the induced Brönsted acid sites has also been discussed.