超大孔Fe和V－Ti分子筛的合成

水热法合成了具有超大孔ＭＣＭ－４１分子筛结构的含Ｐｅ和Ｖ－Ｔｉ分子筛，通过ＸＲＤ、骨架ＩＲ、ＥＳＲ、￣（２９）ＳｉＭＡＳＮＭＲ、紫外漫反射等测试表征证实，Ｆｅ原子在ＦｅＭＣＭ－４１分子筛骨架上，Ｖ和Ｔｉ同时进入Ｖ－ＴｉＭＣＭ－４１分子筛骨架。ＦｅＭＣＭ－４１的骨架红外谱除Ｆｅ分子筛的特征吸收峰６６０ｃｍ￣（－１）外，还显示９６０ｃｍ￣（－１）峰，ＥＳＲ谱出现高对称八面体环境Ｆｅ（Ⅲ）信号（ｇ＝２．０）和扭曲四面体环境Ｆｅ（Ⅲ）信号（ｇ＝４．２），而Ｖ－ＴｉＭＣＭ－４１的骨架红外９６０ｃｍ￣（－１）峰强度分别随分子筛中钛或钒的含量线性增强。约在ｇ＝１．９８处出现的超精细结构ＥＳＲ信号表明Ｖ以分散的不流动的Ｖ￣（４＋）形式存在，化学分析结果表明骨架上Ｔｉ和Ｖ原子相互间不排斥。     

钛硅沸石分子筛TiMCM-41的微波合成与表征

ＭＣＭ４１分子筛是一类以表面活性剂季铵碱或季铵盐为模板剂,液晶模板机理合成,孔道六方有序排列,孔径大小可在１６～１０ｎｍ范围内调节的新颖中孔硅铝分子筛材料．在多相催化、离子交换、吸附分离以及高等无机材料等领域具有较高的工程应用与学术研究价值［１］...     

MCM-41分子筛的合成及129Xe核磁共振的研究

ＭＣＭ４１中孔分子筛是１９９２年由Ｍｏｂｉｌ公司的科学家Ｋｒｅｓｇｅ［１］等人首次合成的,并在《自然》杂志发表。这种中孔分子筛具有六角形孔径,孔径２ｎｍ～１０ｎｍ,这种分子筛的孔径可以通过水晶模板来控制［２］。已报道的合成ＭＣＭ４１,孔径一般在２．０ｎｍ～３．５ｎｍ,使用的水晶模板一般是单一或两种阳离子季铵盐表面活性剂［３,４］。本论文通过引入第二种扩孔模板,与阳离子季铵盐协同作用,合成了孔径５．２ｎｍ（ＢＥＴ法测）的ＭＣＭ４１。通过氮气的吸脱附,测定了分子筛的比表面和孔径等性质。Ｊ．Ｆｒａｉｓｓａｒｄ…     

MCM—41中孔分子筛修饰电极对铁（Ⅱ）和钌（Ⅱ）的1,10—氮 …

用循环伏安法研究ＭＣＭ－４１分子筛修饰电极对铁（Ⅱ）和钌（Ⅱ）的１，１０＝氮杂菲配合物的电化学行为，由于ＭＣＭ－４１中孔分子筛孔表面存在非常活泼的羟基，使其具有很高的活性，它能使分子筛本身作为配体与金属离子配位，并便原来的配体部分解离。     

晶化温度对MCM-41结晶度、酸性和骨架铝结构的影响

选择硅酸钠－硫酸铝－十六烷基三甲基氯化铵体系,在水热条件下合成ＭＣＭ－４１中孔分子筛,采用ＸＲＤ、ＩＲ、ＮＨ３－ＴＰＤ、２７Ａｌ－ＭＡＳＮＭＲ进行了晶化温度与ＭＣＭ－４１分子筛结构和性能的关联研究．结果表明,在晶化温度为１５０℃时,ＭＣＭ－４１分子筛的结晶度最高;适当提高晶化温度,ＭＣＭ－４１分子筛呈现出酸性增加、四铝配位环境趋于规则和弱酸中心逐渐消失的规律．     

MCM-41中孔分子筛修饰电极对铁(Ⅱ)和钌(Ⅱ)的1,10-氮杂菲配合物的电化学响应

用循环伏安法研究ＭＣＭ－４１分子筛修饰电极对铁（Ⅱ）和钌（Ⅱ）的１，１０－氮杂菲配合物的电化学行为．由于ＭＣＭ－４１中孔分子筛孔表面存在非常活泼的羟基，使其具有很高的活性，它能使分子筛本身作为配体与金属离子配位，并使原来的配体部分解离．     

高硅分子筛MCM-41热稳定性与水热稳定性的初步研究

高硅分子筛ＭＣＭ－４１热稳定性与水热稳定性的初步研究董维阳,龙英才,郜晓琴,许太明,谢关根,高滋（复旦大学化学系,上海,２００４３３）关键词高硅分子筛ＭＣＭ－４１,热稳定性,水热稳定性,环己烷吸附等温线ＭＣＭ－４１是最近几年刚刚发现的中孔分子筛（Ｍ４...     

晶化温度对中孔分子筛（M41S）结构转变的影响

在低表面活性剂浓度及低表面活性剂与氧化硅比的条件下，研究了十六烷基三甲基溴化铵－硅酸钠体系中晶化温度对中孔分子筛Ｍ４１Ｓ材料结构转变的影响。结果有，晶化温度提高至１３５℃改变了原六方晶相ＭＣＭ－４１的结构，晶化温度提高到１５０℃后，中孔结构六方ＭＣＭ－４１晶格转变为变不稳定的层状相，     

Cu修饰的MCM—41的合成,表征及对芳烃羟化反应催化作？…

利用ＭＣＭ－４１形成过程中协同自组装特点,在合成过程中引入Ｃｕ（ＮＨ３）４＾２＋,制备出过渡金属表面修饰的纯硅介孔分子筛Ｃｕ－ＭＣＭ－４１,采用ＸＲＤ,ＩＣＰ,ＥＳＲ,Ｎ２吸附等手段确定Ｃｕ处于ＭＣＭ－４１的表面,取代了端羟基中氢的位置,与骨架桥氧和硅羟基中的氧配位,利用苯酚羟化反应为探针,考察了Ｃｕ－ＭＣＭ－４１的催化活性。结果表明,Ｃｕ－ＭＣＭ－４１具有很高的苯酚羟化活性,与ＴＳ－１分子筛的催     

杂原子HMS介孔分子筛的催化脱氢和加氢脱硫性能

ＭＣＭ４１［１］和ＨＭＳ［２］等介孔分子筛对大分子的扩散阻力较小且具有良好的热稳定性,特别是在合成中可以直接将各种杂原子引入骨架,从而调变其催化性能,因此目前介孔分子筛在催化中的应用引起了各国研究者的广泛兴趣．Ｔｉ,Ｚｒ,Ｖ,Ｃｒ,Ｍｎ,Ｃｕ和Ｆｅ...     

Studies of Acid Properties of FeSiMCM-41 and LaSiMCM-41 by NH3-microcalorimetric and NH3-TPD Measurements

The acidity of mesoporous materials FeSiMCM-41, LaSiMCM-41, SiMCM-41, AlSiMCM-41 and HAlSiMCM-41 has been investigated by microcalorimetric studies of the adsorption of ammonia and temperature programmed ammonia desorption method. In the initial stage, the acid strength sequence is SiMCM-41>HAlSiMCM-41>AlSiMCM-41>FeSiMCM-41>LaSiMCM-41, in agreement with that found for microporous molecular sieves materials. A small number of strong acid sites of SiMCM-41 may result from the aluminum impurity contained in the silica source material. The acid density sequence is HAlSiMCM-41>AlSiMCM-41>FeSiMCM-41>LaSiMCM-41SiMCM-41 and can be explained by the studies of existing states of trivalent atoms in these samples reported in previous work. Since some NH₃-TPD plots of these samples show the profiles that could not be back to baseline at elevated temperature, the technique of microcalorimetric adsorption is preferable in studying these samples.This revised version was published online in November 2005 with corrections to the Cover Date.     

Co掺杂SAPO-5分子筛制备及其催化氧气氧化环己烷反应性能(英文)

环己醇和环己酮(KA油)是制备尼龙所需材料己二酸和己内酰胺的重要中间体,也可用作油漆、农药和染料等的溶剂以及染色和褪光丝的均化剂等.工业上制取KA油的方法主要为苯酚加氢法、环己烯水合法和环己烷氧化法,其中环己烷氧化法最为普遍,是非常重要的工业过程.为获得适宜的KA油选择性,工业上普遍采用Co盐为催化剂,将环己烷氧化单程转化率控制在5.0%以下,从而使得产物选择性达到70%以上.该环己烷氧化制KA油过程不仅生产效率较低,而且所用均相催化剂因分离困难而不能重复使用.因此,当前关于环己烷氧化反应催化剂的研究均是围绕多相催化剂进行.氧气选择性氧化环己烷反应因具有更高的原子经济性而逐渐成为环己烷氧化法制KA油研究中最具挑战性的课题.该反应是自由基机理,而Co~(2+),Cr~(3+),Mn~(2+)和Ce~(2+)等金属离子可以促进自由基链反应,因此含有这些金属的多相催化剂被广泛用于该反应.另一方面,AlPO-n系列分子筛由于具有特殊的孔结构和一定的表面酸性,在催化反应中显示出较大的应用潜力.如果进行杂原子掺杂,通过改变分子筛骨架的电荷平衡,可以有效提高其表面酸性.例如磷酸硅铝分子筛(SAPO-5)具有中等强度的酸性和良好的择形性,因而作为固体酸催化剂广泛用于乙醇脱水、甲醇制烯烃、丙烯聚合和苯乙烯环氧化等反应,表现出较高的选择性和良好的稳定性.本文以传统均相Co盐催化剂的多相化为出发点,制备了Co掺杂SAPO-5与分子筛催化剂(Co-SAPO-5),考察了Co掺杂量对催化剂结构、表面性质以及氧气选择性氧化环己烷反应性能的影响.结果表明,一部分Co进入分子筛骨架,同时有少量Co以氧化钻形式高度分散在SAPO-5表面.Co掺杂对SAOP-5催化剂比表面积没有显著影响,但可使其孔体积减小.相反,Co掺杂可以提高SAOP-5分子筛表面B酸性位数量和总酸量.活性测试结果表明,环己烷转化率随着Co-SAPO-5催化剂中Co含量的增加而增加,但KA油选择性在转化率高于6.3%时急剧下降.还考察了反应温度、反应时间、初始氧气压力和催化剂用量对Co-SAPO-5分子筛催化剂性能的影响,得到了最优反应条件.以Co-SAPO-5-0.2(Co/Si摩尔比为0.2)分子筛为催化剂时,KA油总收率最高可达7.8%.另外,Co-SAPO-5催化剂在环己烷氧化反应中显示出很好的稳定性,Co-SAPO-5-0.2催化剂套用6次后活性几乎没有变化.     

Thermodynamics of CO probe molecule adsorption on Cu–FER-zeolite comparison of TPD,FTIR, and microcalorimetry results

The existence of the new type of the adsorption complexes of carbon monoxide, where CO molecule interacts simultaneously with both copper and potassium cation, formed on so-called heterogeneous dual adsorption sites was detected by the FTIR spectroscopy and temperature programmed desorption technique (TPD) in the Cu, K–FER zeolite samples. The time-resolved IR spectroscopy and TPD experiments also proved their lower stability in the comparison with the classical monodentate adsorption complexes. The TPD curves of these materials exhibited low temperature desorption peak which was ascribed to these sites. The energetic parameters (i.e., energy and entropy of adsorption) as well as distribution of all present Cu⁺ sites were obtained by the fitting of TPD data to the phenomenological model. Obtained results suggest that the heterogeneous dual sites are special form of the adsorption sites localized on the wall of channels destabilized due to significantly higher change of the entropy of adsorption. Direct microcalorimetric measurement proved energetic equality of single and heterogeneous dual sites together with the validity of the adsorption energy values obtained from TPD.     

SAPO分子筛的酸性及其孔道分布对丁烷异构脱氢反应的影响

 合成了四种磷铝及硅磷铝系列分子筛,并用XRD表征了分子筛的晶体结构,用X荧光光谱测定了其元素组成,用NH3－TPD和物理吸附考察了其酸性和孔道分布．考察了以合成的分子筛为基质制备的催化剂上丁烷异构脱氢反应的性能．结果表明,以弱酸性的SAPO－5分子筛和孔口狭窄的SAPO－34分子筛为载体的催化剂,它们的催化性能较差;以十元环的SAPO－11分子筛为载体的催化剂显示出较高的活性和选择性．同时,考察了不同分子筛催化剂上Pd金属粒子的分散状态,分析了分子筛的酸性和孔道结构对反应性能的影响．     

金属取代型AlPO-5分子筛催化剂上环己烷亚硝化一步法合成己内酰胺(英文)

采用水热法制备了一系列结晶态的AlPO-5(磷酸铝分子筛),SAPO-5(硅磷酸铝分子筛)和MeAlPOs(金属取代型磷酸铝分子筛)催化剂,利用X射线衍射、N2吸附脱附法、扫描电镜、粒度分布、电感耦合等离子光谱、红外光谱、NH3程序升温脱附、H2程序升温还原和热重-微分热重分析对催化剂进行了表征,并考察了其催化环己烷亚硝化一步法制备己内酰胺的反应活性.结果表明,随着Si或金属原子引入AlPO-5结构中,催化剂的Lewis弱酸中心增加,同时出现了Brnsted强酸中心.相对于AlPO-5,具有较大比表面积和较多酸中心的SAPO-5和CrAPO-5表现出较好的环己烷亚硝化反应活性,后者环己烷转化率为8.16%,己内酰胺选择性达68.17%.     

Synthesis, characterization, and catalytic properties of stable mesoporous molecular sieve MCM-41 prepared from zeolite mordenite

Mesoporous molecular sieves (denoted as M-MCM-41) with ordered hexagonal structure have been successfully synthesized from the assembly of precursors from preformed zeolite Mordenite with CTAB surfactant micelle in alkaline media. The samples were characterized by XRD, N₂ adsorption, IR and DTG. The materials exhibit highly hydrothermal stability, as compared with conventional MCM-41. Characterization results indicate that the mesoporous walls of M-MCM-41 contain the secondary building units similar to those in microporous crystal of zeolite Mordenite. In catalytic dealkylation of C10⁺ aromatic hydrocarbon, M-MCM-41 shows higher activities in comparison with Mordenite and MCM-41, which would be ascribed to the combination of advantages of both MCM-41 (large pores) and Mordenite (strong acidity). Furthermore, this synthesis strategy could be used as a new general method for the preparation of hydrothermally stable mesoporous aluminosilicate materials under alkaline conditions.     

Preparation, Characterization and Catalytic Performance of La-SO42-/SBA-15 in Esterification of Acetic Acid with n-Butanol

La-SO42-/SBA-15 was synthesized with various amounts of lanthanum via incipient-wetness impregnation.Characterization was done by X-ray diffraction(XRD), transmission electron micrographs(TEM), nitrogen adsorption,FTIR spectroscopic analysis, thermogravimetric analysis, and the total amount of acidity of catalyst was estimated by TPD of NH3. The results indicate that lanthanum has been incorporated into SBA-15 molecular sieve. The prepared materials(La-SO42-/SBA-15) keep the highly ordered mesoporous two-dimensional hexagonal structure and do not change the mesoporous channel structure of the support SBA-15. The catalyst showed best catalytic activity in the synthesis of n-butyl acetate. The optimum conditions of the esterification by orthogonal experiments were studied: the molar ratio of n-butanol to acetic acid 1:1.2, the amount of catalyst 7.5%, reaction time 80 min. The yield of n-butyl acetate could reach 93.2% under the optimum conditions. The catalyst was recyclable, cost effective and environmental friendly.     

MCM-41负载钨磷杂多酸催化剂的性能研究

制备并表征MCM-41负载H~3PW~1~2O~4~0(PW)催化剂.PW杂多酸在MCM-41上负载量高达70%(质量分数)时,XRD中仍未检测到其晶相峰.PW杂多酸与MCM-41载体的相互作用要比与SiO~2载体的强.PW杂多酸中的质子位是非常强的酸中心,它们对NH~3的微分吸附热在160-180kJ/mol的范围.与PW杂多酸相比,PW/MCM-41催化剂的酸中心强度变弱并且分布不均匀,其酸量和酸中心分布可以通过改变PW杂多酸的负载量来调节.PW/MCM-41是一类适合于中强酸和弱酸催化反应的新型固体酸催化剂。     

水解对MCM-41分子筛的结构破坏作用

详细考察了ＳｉＭＣＭ－４１、ＡｌＭＣＭ－４１和ＨＡｌＭＣＭ－４１在不同环境中的水解和结构破坏情况．空气和水蒸汽中短期高温焙烧对全硅型ＳｉＭＣＭ－４１的结构影响较小,但在潮湿空气中长期放置可因Ｓｉ—Ｏ—Ｓｉ键发生水解而造成结构的严重破坏．ＡｌＭＣＭ－４１的抗水解能力优于ＳｉＭＣＭ－４１的,但因其结构中包含一定量的Ｎａ＋离子,降低了高温焙烧时结构的热稳定性和水热稳定性．ＨＡｌＭＣＭ－４１的热稳定性和水热稳定性均优于ＡｌＭＣＭ－４１．分子筛水热晶化过程中的盐析效应被证实是导致ＡｌＭＣＭ－４１和ＨＡｌＭＣＭ－４１抗水解能力增强的原因,因此在合成原料中加盐可显著改善ＭＣＭ－４１分子筛的抗水解能力和稳定性