不同硅烷对HMS介孔分子筛甲基接枝的对比研究

通过气相沉积法,分别用三甲基氯硅烷(TMCS)和六甲基二硅氮烷(HMDSZ)对HMS介孔分子筛表面进行甲基接枝改性;分别采用XRD、N2-吸附、FTIR、29SiNMR和TG等手段对样品进行表征,并测定了样品的亲水性能.结果表明,两种硅烷都可以在HMS表面接枝,接枝后分子筛的介孔结构依然保持;但是,HMDSZ的接枝效果...     

化学气相沉积法制备Ti/HMS催化剂及甲基接枝改性

用化学气相沉积法制备了Ti/HMS介孔分子筛催化剂, 并对其进行甲基接枝改性. 用XRD、N2-吸附、ICP-AES、FTIR, UV-vis和29Si CP/MAS NMR等手段对样品进行了表征, 考察了催化剂的丙烯环氧化性能. 结果表明: 气相沉积法载钛和接枝改性减小了HMS分子筛表面的孔径和比表面, 但是分子筛的介孔特征仍然保持; 随着沉积时间的增加(0.5～2 h), 催化剂的钛含量逐渐增加, 催化活性也随之增加, 但当沉积时间超过2 h后, 钛含量和催化活性均保持不变; 接枝改性后催化剂的环氧化活性和选择性均显著提高; 气相沉积法合成Ti/HMS比水热法合成Ti-HMS具有更高的环氧化催化活性.     

后合成Ti/HMS催化剂的表征及对丙烯的催化环氧化性能研究

以正硅酸乙酯为硅源,正十六胺为模板剂,乙醇和水为溶剂,采用水热合成法制备了纯硅HMS介孔材料.以TiCl4为钛源,采用气相接枝技术将Ti物种引入到HMS的骨架中,制得Ti/HMS催化剂;以六甲基二硅氮烷为硅烷化试剂,采用液相接枝技术,将甲基接枝到Ti/HMS催化剂表面,以提高催化剂的疏水性.采用XRD、N2吸附、TEM、UV-Vis和FT-IR等技术表征研究了催化剂的结构、表面化学组成及疏水性;以过氧化氢异丙苯为氧化剂,分别在淤浆床及固定床反应器中,研究了Ti/HMS催化剂对丙烯的催化环氧化性能及稳定性.研究结果表明,所制备的Ti/HMS催化剂具有典型的六方介孔结构特征,且钛物种主要以四配位的活性物种形式存在于骨架中;经硅烷化试剂处理后,催化剂的疏水性得到显著提高;经硅烷化处理后的催化剂对丙烯环氧化具有优异的活性、选择性和稳定性,在2400小时的稳定性实验中,CHP的转化率维持在99.0%以上,环氧丙烷的选择性维持在97.0%以上.     

甲基接枝化HMS介孔分子筛的制备、表征与吸附性能

以工业级正十六胺为模板剂合成纯硅HMS介孔分子筛,用液相沉积法、以环己烷为溶剂对其进行表面接枝改性,并用简单的热失重分析法确定了最佳的硅烷浓度:通过IR、29SiCP-MAS NMR、XRD和N2吸附等手段对样品进行表征,考察了样品的吸附性能.结果表明,甲基成功接枝于HMS表面,最佳的硅烷用量为0.23mol/L,甲基接枝后HMS的孔径和比表面有所降低;接枝后HMS的吸附水性能(亲水性)大幅度降低,而吸附环己烷性能(亲油性)大幅增加.     

双亲型Ti/ZSM-5分子筛催化剂的制备及氧化脱硫性能

通过使用二苯基硅烷和氨丙基三乙氧基硅烷对Ti/ZSM-5分子筛进行非对称修饰, 获得了外侧亲油、 内侧亲水的双亲型催化剂材料am-Ti/ZSM-5. 修饰过程及后处理过程并未破坏分子筛的骨架结构. 样品在不添加萃取剂的情况下, 在以H₂O₂为氧化剂的二苯并噻吩(DBT)氧化脱硫(ODS)反应中表现出高催化活性, 在35 min内可以实现模拟油中DBT的完全脱除. 实验结果表明, 分子筛催化剂的双亲型结构使其在极性-非极性混合体系中具有优异的催化性能.     

钒改性六方介孔硅分子筛催化苯羟基化制苯酚

以偏钒酸铵为钒源,采用溶胶-凝胶法合成了不同钒含量的六方介孔硅（V-HMS）分子筛,利用X射线衍射、N2吸附-脱附和程序升温还原(H2-TPR)对合成的催化剂进行了表征,考察了V-HMS对苯羟基化反应的影响。 结果表明,钒进入了分子筛骨架,并且在HMS分子筛上具有较好的分散性。 V-HMS对苯羟基化反应具有良好的催化活性;高分散的钒氧物种有利于提高苯的羟基化反应性能,溶剂乙腈对反应促进作用明显。 乙腈为溶剂,w(V(5.8)-HMS)=2%,60 ℃反应5 h,苯酚收率达到18.55%,选择性达到100%。     

不同硅铝比的MCM-22分子筛的气相硅烷化处理

对不同硅铝比的MCM-22分子筛进行气相硅烷化处理,并采用X射线衍射、固体核磁、N₂吸附-脱附和甲苯吸附等技术对样品进行了表征. 结果显示,原料硅铝比为50~100的MCM-22分子筛均可以利用气相硅烷化,在不脱除骨架铝的基础上,将Si(OH)₂柱撑结构引入其层间超笼系统,从而使层间距增大,孔体积增加; 将密度泛函理论用于计算硅烷化前后的MCM-22分子筛的N₂吸附等温线,成功得到十元环孔道和超笼体系的比表面积和孔体积,发现气相硅烷化使MCM-22分子筛超笼体系的比表面积和孔体积增大,而十元环孔道减小.另外,气相硅烷化可有效提高不同硅铝比MCM-22分子筛的甲苯平衡吸附量.     

无机SiO2-TiO2前驱体体系合成高性能TS-1分子筛

 在热处理条件下,使Ti(SO4)2在多孔硅胶表面自发分散形成具有类似于钛硅分子筛催化活性中心结构单元的Si-O-Ti键的SiO2 -TiO2前驱体,将该前驱体在模板剂四丙基氢氧化铵的作用下水热晶化得到了钛硅分子筛TS-1. X射线衍射、红外光谱和扫描电镜表征表明, TS-1分子筛晶化完全,钛原子已进入TS-1分子筛骨架. 苯酚羟基化反应测试结果表明,前驱体的热处理温度对合成的TS-1分子筛的催化性能影响很大,处理温度以450 ℃为宜.     

四氯化钛气固相反应法制备钛硅分子筛机理的研究

采用气固相法使TiCl₄与HZSM-5高硅分子筛反应制备了钛硅分子筛Ti-ZSM-5.运用FT-IR, UV-vis, XRD, TG, ICP-AES等手段对合成的钛硅分子筛进行了表征,并以30%H₂O2水溶液环氧化氯丙烯为探针反应对合成的Ti-ZSM-5进行了催化活性考察,结果表明分子筛所载钛原子完全进入骨架,没有发现非骨架钛,Ti-ZSM-5催化性能良好. 定量分析结果表明,钛原子同晶取代铝原子反应进入骨架的贡献极小,仅占骨架钛的0.32%,钛原子主要通过TiCl₄与羟基窝反应而进入分子筛骨架.     

含Ti的HMS介孔材料催化剂及其对丙烯环氧化催化性能的研究

分别用水热合成法和气相四氯化钛(TiCl4)接枝法制备了Ti-HMS和Ti/HMS催化剂.表征结果表明,经过气相TiCl4接枝后的样品依然保持HMS(Hexagonal Mesoporous Silica,缩写为HMS)介孔材料特征,钛(Ti)物种主要以四配位的活性位形式存在.经过甲基接枝处理的催化材料,增加了表面的疏水性.丙烯环氧化反应结果表明,SN-Ti/HMS具有更高的催化性能.在2 500 h的稳定试验中,过氧化氢异丙苯(CHP)转化率大于99.0%,环氧丙烷(PO)选择性大于96.0%.研究和优化了环氧化反应工艺条件.采用浓度为30%的CHP为原料,CHP重量空速为1.0 h-1,床层温度为100℃,反应压力为3.0 MPa.     

Characterization and catalytic performance of methyl-grafted Ti-HMS catalysts prepared by the CVD method

Methyl-grafted Ti-HMS catalysts were prepared by the chemical vapor deposition (CVD) method using TiCl₄ as titanium source and various organic silanes as silylating agents. The catalysts were characterized by XRD, N₂-adsorption-desorption, FTIR, ²⁹Si NMR, TGA, DR UV-vis, and evaluated by the epoxidation of propylene using cumene hydroperoxide (CHP) as oxidant. The results reveal that the silylated Ti-HMS catalysts are more active than the unsilylated Ti-HMS catalyst, and the methyl-grafted Ti-HMS catalyst silylated with hexamethyldisilazane (HMDSZ) exhibits better epoxidation performance than the analogues silylated with trimethylchlorosilane (TMCS) or dimethyldichorosilane (DMDCS). It is proposed that not only the form of T-O-SiMe_n (n = 2 or 3) but also the breakage of Ti-O-T (Si-O-Si or Si-O-Ti) are observed in silylation using Cl-containing silylating agents (TMCS or DMDCS), which decrease the hydrophobicity of Ti-HMS catalysts and destroy the tetracoordinated titanium species that responsible for the epoxidation performance. This phenomenon has not been observed in silylation with HMDSZ.     

Comparative Study of Titanium-modified HMS Mesoporous Materials via Different Preparing Methods

The current work is focused on the testing of titanium modified hexagonal mesoporous silica (HMS) for catalysts in epoxidation of cyclohexene. Two samples were prepared via the chemical liquid deposition (CLD) and the chemical vapor deposition (CVD), namely Ti/HMS-L and Ti/HMS-V, respectively. HMS and Ti/HMS were characterized by XRD, N₂-adsorption, ICP-AES, UV-Vis. The samples were also evaluated by the epoxidation of cyclohexene with cumene hydroperoxide (CHP) as oxidant. It is revealed that Ti/HMS samples possess typical hexagonal mesoporous structure in which most of titanium species exist in the form of framework tetracoordinated state. Meanwhile, Ti/HMS-V is more seriously affected than Ti/HMS-L since the former was prepared at higher temperature. Ti/HMS-V gives more excellent catalytic performance than Ti/HMS-L, which is likely because the former has more isolated and framework titanium species. Either Ti/HMS-V or Ti/HMS-L can be used only 1 time in epoxidation experiment.     

Characterization of silylated Ti-grafted HMS catalyst and its excellent epoxidation performance

Silylated Ti-grafted hexagonal mesoporous silica (HMS) catalyst was prepared by the chemical vapor deposition (CVD) using TiCl4 as titanium source and hexamethyldisilazane (HMDSZ) as silylating agent. The samples were characterized by XRD, N2- adsorption, FTIR, 29Si NMR, DR UV-vis, and evaluated by epoxidation of styrene, propylene, cyclohexene, and 1-hexene with cumene hydroperoxide (CHP) as oxidant, respectively. It is revealed that the catalyst possesses typical mesoporous structure, high hydrophobicity and highly dispersed tetracoordinated titanium sites and hence exhibits excellent performance in epoxidation of olefins.     

Effect of silylation temperature on the physicochemical properties and catalytic performance of Ti-containing hexagonal mesoporous silica

Russian Journal of Applied Chemistry - Ti-HMS (hexagonal mesoporous silica, HMS) was vapor silylated at 150–450°C. The samples were characterized by Si29 CP/MAS NMR, FTIR, TG, XRD, and...     

HMS和NaY固载酒石酸钛配合物的研究

利用化学键合和“瓶中造船”方法,成功地将酒石酸钛配合物接枝到HMS(heragonal mesoporous silicas)上或包络合于微孔NaY内.FT-IR表征表明酒石酸钛在HMS上是通过与载体表面羟基发生交换作用而被固载的;在NaY载体上则是通过包络合被封装在载体的超笼内.UV-Vis可见漫反射表征表明两类固载型催化剂有着相似的钛配位环境.在催化肉桂醇环氧化反应中,HMS键合型催化剂的反应转化率比NaY包络型催化剂的高;但后者在环氧化选择性上要高于前者.回收样品的重复使用实验结果表明,两类固载型催化剂在重复使用过程中均存在不同程度的失活.     

A study in high-temperature silylation of silica

High-temperature silylation (HTS) used for the deactivation of capillary columns was studied on the silica commonly used in HPLC to gain a better insight into this process. LiChrosorb Si 100 was silylated with disilazanes at different temperatures and the materials obtained were compared in terms of organic and silanol group surface concentration, IR reflection spectra, HPLC behavior, and pore distribution parameters. Applying diphenyltetramethyldisilazane, the volatile reaction products were monitored during the HTS process. With increasing silylation temperature up to 400°C the silanol surface concentration is reduced to a very small level independent of the organic group concentration which exhibits a broad maximum depending upon substituents and temperature. Up to 350°C triorganosiloxy groups prevail as bonded organic groups. It could be proved that HTS is accompanied by pore alterations of the silica matrix. Arguments proposed by different authors in explaining HTS effects are discussed.     

Ti-HMS介孔分子筛的制备及其在一氧化氮催化分解反应中的活性

 在常温下制备了具有不同钛含量的大比表面积和孔体积的介孔分子筛HMS．XRD谱表明,这些Ti－HMS样品呈现出很好的六方晶形．经焙烧后,Ti－HMS样品的UV吸收光谱和XAFS谱结果表明,在Ti－HMS（1）和Ti－HMS（2）骨架中的钛离子以四配位存在,而在Ti－HMS（10）中至少有部分钛是以六配位存在．在NO存在的情况下,在273K下光催化剂Ti－HMS受紫外光照射后,导致NO分解生成N2,O2和N2O．实验结果表明,具有高分散四配位钛的Ti－HMS（1）使NO以高效率、高选择性分解生成N2和O2;随着钛含量的增加,其光催化活性反而降低．     

Anwendung3H-markierter Silylierungsmittel zur Bestimmung der Geschwindigkeits- und Gleichgewichtskonstanten der Silylierungsreaktionen für die massenspektrometrische Analyse von Steroidhormonen

Steroid hormones were silylated, using³H-labelled silylating agents. The trimethylsilyl ether derivatives obtained were stable products. Using HMDS and TMCS the silylation reaction of 3α-hydroxy-5α-androstane was a first order reaction.     

新型WO3/HMS催化剂的制备及其对环戊烯选择氧化反应的催化性能

 采用草酸络合方法将WO3固载到六方介孔全硅分子筛HMS上,制得新型WO3/HMS非均相催化剂. 利用SEM,TEM,N2吸附,XRD及激光拉曼光谱等手段对催化剂进行了表征,研究了催化剂在环戊烯选择性氧化合成戊二醛反应中的催化性能. 结果表明,在WO3/HMS催化下环戊烯和H2O2的转化率均可达100%,戊二醛的选择性可达72%. WO3以高分散状态存在于催化剂表面. 单次反应后钨的溶脱量(5.5 μg/ml)很小,对反应几乎没有影响. 催化剂具有较高的稳定性,可以重复套用6次. 失活后的催化剂可通过简单焙烧的方式再生.     

Silylation of a Co/SiO2 catalyst. Characterization and exploitation of the CO hydrogenation reaction

Several silylated- and nonsilylated Co/SiO2 catalysts have been prepared by reaction of the surface silanol groups with hexamethyldisilazane (HMDS). These samples have been characterized by means of N2 adsorption isotherms, solid-state nuclear magnetic resonance (29Si and 1H), X-ray photoelectron spectroscopy, thermogravimetric analysis, and diffuse reflectance IR spectroscopy. We have focused on the study of the silylated surface stability at high temperatures and in different atmospheres. The characterization techniques have shown that silica silylation after cobalt impregnation leads to a silylated SiO2 surface composed of hydrophobic Si-(CH3)3 species highly stable up to 600-650 K in both oxidizing and reducing atmospheres. However, X-ray diffraction and temperature-programmed reduction have shown that the hydrophobic nature of the silica surface does not affect the metal dispersion and its reducibility. The materials prepared in this way have been tested as catalysts for the Fischer-Tropsch synthesis reaction. The CO conversion reaction rate increased over the silylated catalyst, probably as a consequence of the higher number of available active sites because water adsorption over the catalyst surface is impeded. However, catalyst deactivation was not affected by the hydrophobic nature of the support, suggesting that carbon deposition is the more probable mechanism of cobalt-based catalyst deactivation during the Fischer-Tropsch synthesis.