Co-MCM-41催化剂上临CO2-乙烷脱氢反应的研究

合成了不同Co掺杂量的Co-MCM-41分子筛.用XRD,FTIR和TG-DTA等技术对所制样品进行表征.在常压连续流动固定床反应器上考察了它们对临CO₂-乙烷脱氢制乙烯反应的性能,结果表明,3%Co-MCM-41在973K可使乙烷的转化率达到39.54%,乙烯的选择性达到98.59%,收率达到38.98%.Co的掺杂量和反应温度等条件对该反应均有一定影响.Co-MCM-41对乙烷催化脱氢制乙烯同样也有很高的活性.引入CO₂可消除积炭对催化剂活性的影响,更有利于催化反应的进行.     

纳米Cr2O3的制备、表征及催化性能

首次采用溶胶-凝胶法与共沸蒸馏法耦合技术制备了纳米Cr2O3粉体，并运用BET、TEM、XRD、FT-IR、XPS及H2-TPR对其进行表征，同时采用CO2氧化乙烷脱氢制乙烯反应作为探针反应，考察了纳米Cr2O3的催化性能。首次发现纳米ErgO3的FT-IR谱出现了蓝移现象，并且630cm^-1附近的伸缩振动峰强度增强。初步探讨了纳米氧化物的IR蓝移和红移的原因，指出晶型是影响纳米氧化物红外光谱特征的重要因素。实验结果表明纳米Cr2O3上乙烷和CO2转化率均明显高于常规Cr2O3催化剂；在700℃下，乙烷转化率高达77．1％，而乙烯产率达到了58．98％。     

BO3－3／Mo－MCM－41的制备及其对2－甲氧基萘乙酰化反应的催化性能

 制备了Mo－MCM－41中孔分子筛，并将BO3－3引入到分子筛中制得BO3－3／Mo－MCM－41催化剂．采用XRD，FT－IR，ESR，BET和NH3－TPD对分子筛催化剂的结构及酸强度进行了表征．结果表明，Mo－MCM－41和BO3－3／Mo－MCM－41具有中孔分子筛的特征，有良好的长程有序 性和结晶度；但Mo并未进入分子筛骨架内部而是在分子筛表面以MoO2的形式存在；BO3－3附着于Mo－MCM－41分子筛上形成强酸中心．将BO3－3／Mo－MCM－41用于催化2－甲氧基萘乙酰化反应，考察了催化剂用量、Si／Mo比及BO3－3的引入方式对该反应性能的影响，发现BO3－3／Mo－MCM－41对2－甲氧基萘乙酰化反应具有良好的催化性能．     

高硅分子筛ZSM-23催化裂解C4烷烃制乙烯丙烯的研究

采用廉价的硅溶胶作为硅源,吡咯烷为模板剂,静态水热晶化法合成出不同硅铝比的ZSM-23分子筛.采用XRD,SEM,吡啶吸附红外光谱等技术,对合成的ZSM-23分子筛的结构、形貌、表面酸性质进行了表征.并进行了所制样品对C4烷烃催化裂解制乙烯丙烯反应催化性能的研究.本文详细考察了硅铝比、反应温度、反应空速以及催化剂稳定性等各种因素对催化性能的影响.结果表明,ZSM-23分子筛的乙烯丙烯收率达到56.0%,丁烷转化率达到88.9%.     

MCM-41表面羟基与四新戊基锆的反应

四新戊基锆(ZrNp4)能在室温下与MCM 41分子筛表面羟基发生化学反应,导致=ZrNp2基团通过两个氧原子接枝在分子筛的表面.文章介绍了这种表面化合物的制备方法,考察了反应温度、ZrNp4升华温度以及MCM 41脱水温度对制备的影响, 并用红外、固体魔角自旋核磁共振、化学探针反应表征了表面有机金属化合物的组成和结构.     

纳米Cr2O3系列催化剂上CO2氧化乙烷脱氢制乙烯反应

 采用溶胶－凝胶法和共沸蒸馏法耦合技术制备了纳米Cr2O3催化剂，并采用共沉淀法和共沸蒸馏法耦合技术制备了纳米Cr2O3／Al2O3，Cr2O3／ZrO2和Cr2O3／MgO复合催化剂．应用BET，XRD，XPS，TPR和TEM等物理化学方法对催化剂的结构和物化性质进行了表征，并考察了该系列催化剂上CO2氧化乙烷脱氢制乙烯的反应性能．结果表明，纳米Cr2O3催化剂上乙烷和CO2的转化率均明显高于常规Cr2O3催化剂，但乙烯的选择性低于常规Cr2O3催化剂；纳米复合催化剂中的复合成分显著影响催化剂的催化性能．其中，10％Cr2O3／MgO纳米复合催化剂在温度为973K时，乙烷转化率和乙烯选择性分别可达到61．54％和94．79％．纳米催化剂表面Cr的还原性以及Cr6＋／Cr3＋比值是影响乙烷转化率和乙烯选择性的重要因素．     

HMI体系下系列沸石子筛的动态合成与表征

在HMI体系中，采用水热动态晶化法，通过对Si/Al比，碱度，晶化温度，晶化 时间等反应条件进行调变，合成出纯相的MOR，ANA，MCM－56，MCM－49和MCM－22 等多种结构的沸石分子筛，发现反应物Si/Al比决定合成产物的物相，通过XRD， TG－DTA，SEM和TEM等方法研究了分子筛的物理化学性质并对HMI体系中合成的MOR 和ANA的晶体特征进行了表征分析。     

HMI体系下系列沸石子筛的动态合成与表征

在HMI体系中，采用水热动态晶化法，通过对Si/Al比，碱度，晶化温度，晶化 时间等反应条件进行调变，合成出纯相的MOR，ANA，MCM－56，MCM－49和MCM－22 等多种结构的沸石分子筛，发现反应物Si/Al比决定合成产物的物相，通过XRD， TG－DTA，SEM和TEM等方法研究了分子筛的物理化学性质并对HMI体系中合成的MOR 和ANA的晶体特征进行了表征分析。     

负载型Co-Cr氧化物催化剂上CO2氧化乙烷脱氢制乙烯反应的研究

制备了一系列不同Co／Cr比例的Co-Cr／SiO2和Co-Cr／γ-Al2O3催化剂，并应用XRD等技术对所制样品进行了表征．在常压连续流动固定床石英反应器中考察了它们对CO2乙烷氧化脱氢反应的催化性能．实验结果表明，Co-Cr／SiO2和Co-Cr／γ-Al2O对CO2乙烷脱氢制乙烯都有较高的催化活性，其活性都明显高于负载单一组分的催化剂．以γ-Al2O为载体的催化剂活性明显比以SiO2为载体的催化剂活性高．1％Co-5％Cr／γ-Al2O活性最高，973K乙烷的转化率达25．57％，乙烯的选择性和收率分别达94．28％、24．10％．     

溶胶-凝胶法制备Cr-基催化剂及其CO2氧化乙烷制乙烯

以硝酸铬为Cr源,正硅酸乙酯为Si源,采用溶胶-凝胶法制备了Cr质量分数为2.5%~10%的Cr-基催化剂;采用XRD、BET、SEM、H₂ TPR等分析测试技术对催化剂的结构进行了表征;在微型固定床反应器中对催化剂乙烷二氧化碳氧化脱氢制乙烯的催化性能进行了评价,并考察了反应条件对催化性能的影响。结果表明,催化剂中Cr的质量分数大于5%时,Cr的物相为Cr₂O₃,但Cr质量分数较低时,检测不到Cr的物相;Cr质量分数为5%的催化剂具有较大的比表面积,Cr质量分数变大或变小,催化剂的比表面积都会减小;催化剂的孔径在2nm左右,并与Cr的质量分数关系不大;Cr质量分数为5%的催化剂具有最好的催化活性,在750℃的反应条件下,乙烷和二氧化碳的转化率可达79.29%和23.74%,乙烯的收率可达67.91%;Cr质量分数为5%的催化剂具有适宜的氧化还原性能,这有利于乙烷和二氧化碳的转化。     

Synthesis, spectroscopy and catalysis of

Chromium acetyl acetonate [Cr(acac)3] complexes have been grafted onto the surface of two mesoporous crystalline materials; pure silica MCM-41 (SiMCM-41) and Al-containing silica MCM-41 with an Si:Al ratio of 27 (AlMCM-41). The materials were characterized with X-ray diffraction, N2 adsorption, thermogravimetrical analysis, diffuse reflectance spectroscopy in the UV-Vis-NIR region (DRS), electron spin resonance (ESR) and Fourier transform infrared spectroscopy. Hydrogen bonding between surface hydroxyls and the acetylacetonate (acac) ligands is the only type of interaction between [Cr(acac)3] complexes and SiMCM-41, while the deposition of [Cr(acac)3] onto the surface of AlMCM-41 takes place through either a ligand exchange reaction or a hydrogen-bonding mechanism. In the as-synthesized materials, Cr3+ is present as a surface species in pseudo-octahedral coordination. This species is characterized by high zero-field ESR parameters D and E, indicating a strong distortion from O(h), symmetry. After calcination, Cr3+ is almost completely oxidized to Cr6+, which is anchored onto the surface as dichromate, some chromate and traces of small amorphous Cr2O3 clusters and square pyramidal Cr5+ ions. These materials are active in the gas-phase and slurry-phase polymerization of ethylene at 100 degrees C. The polymerization activity is dependent on the Cr loading, precalcination temperature and the support characteristics: a 1 wt % [Cr(acac)3]-AlMCM-41 catalyst pretreated at high temperatures was found to be the most active material with a polymerization rate of 14000 g polyethylene per gram of Cr per hour. Combined DRS-ESR spectroscopies were used to monitor the reduction process of Cr(6+/5+) and the oxidation and coordination environment of Cr(n+) species during catalytic action. It will be shown that the polymer chains initially produced within the mesopores of the Cr-MCM-41 material form nanofibres of polyethylene with a length of several microns and a diameter of 50 to 100 nanometers. These nanofibres (partially) cover the outer surface of the MCM-41 material. The catalyst particles also gradually break up during ethylene polymerization resulting in the formation of crystalline and amorphous polyethylene with a low bulk density and a melt flow index between 0.56 and 1.38g per 10 min; this indicates the very high molecular weight of the polymer.     

Effect of synthesis parameters on the chromium content and catalytic activities of mesoporous Cr-MSU-x prepared under acidic conditions

A series of chromium-incorporated MSU-x mesoporous molecular sieves were synthesized under different templates, initial Si/Cr molar ratios, aging times, and temperatures in acid solution. The synthesis was performed by using sodium silicate, chromium nitrate, and nonionic poly(ethylene oxide) surfactant as the source of silicone, metal, and the template, respectively. The Cr-MSU-x products were analyzed by inductively couple plasma-optical emission spectrometry to determine the actual Cr content and were characterized by X-ray diffraction, N(2) adsorption-desorption, scanning electron microscopy, high-resolution transmission electron microscopy, diffuse reflectance UV-visible, X-ray adsorption near-edge spectroscopy, and temperature-programmed reduction techniques. The Cr species were mostly formed as Cr(VI) in tetrahedral coordination. Two kinds of Cr(VI) species with different reduction abilities were distinguished. The catalytic activities of Cr-MSU-x in the dehydrogenation of ethane to ethylene with CO(2) were investigated at the same time. The synthesis parameters explored strongly influence the chromium content in Cr-MSU-x and, subsequently, the catalytic activities. The Cr-MSU-x synthesized with Si/Cr = 20, aging at 25 degrees C for 22 h, and templating by fatty alcohol polyoxyethylene ether gave the best activities, resulting in 58.0% ethane conversion and 92.1% ethylene selectivity. The Cr species in Cr-MSU-x are more efficient in activating and converting ethane molecules than are conventional catalysts.     

MCM-41负载钴催化H_2O_2氧化四氢萘合成α-四氢萘酮

比较了醋酸溶液中过渡金属(Fe、Co、Ni、Ce、Cu、La、Zr或Cr)掺杂MCM-41催化过氧化氢氧化四氢萘合成α-四氢萘酮的转化率和选择性,发现其中Co/MCM-41的催化活性最好。探讨了Co/MCM-41作催化剂时反应温度、反应时间、催化剂用量等对四氢萘氧化的转化率和形成四氢萘酮选择性的影响,确定了较优的反应条件:m(四氢萘)∶m(催化剂)=12.5∶1;反应温度T=383 K,反应时间8 h。四氢萘的转化率达94.7%,α-四氢萘酮的选择性达到70.3%。在反应体系中,Co/MCM-41是一种固体非均相催化剂。催化剂Co/MCM-41可回收重复使用3次,催化活性基本不变。     

微波固相法制备ZnCl2/MCM-41催化剂及其催化性能

采用微波固相法、普通加热法和溶剂分散法等不同方法制备了ZnCl2/MCM-41催化剂,以XRD、FT-IR和TG-DSC等表征手段,比较了不同方法制备的催化剂中ZnCl2在分子筛表面的存在状态.XRD测定结果表明,微波固相法和溶剂分散法制备的样品可使ZnCl2完全分散于MCM-41分子筛表面,而加热法制备的样品中仍存在ZnCl2的晶相衍射峰.FT-IR、DSC和原子吸收光谱的测定结果表明,微波辐射可使ZnCl2与分子筛表面羟基发生固态相互作用形成O－Zn－Cl活性位,具有更加温和的Lewis酸性.考察了不同方法制备和不同ZnCl2负载量的催化剂在月桂烯与丙烯醛Diels-Alder反应中的催化性能,与普通加热法制备的催化剂相比,微波固相法与溶剂分散法制备的催化剂具有更好的催化活性和选择性,但微波固相法制备催化剂更为简单.     

Preparation of H-mordenite/MCM-48 composite and its catalytic performance in the alkylation of toluene with <Emphasis Type="Italic">tert</Emphasis>-butanol

A series of HM/MCM-48 samples with different SiO₂/Al₂O₃ molar ratio were prepared by sol-gel method. The prepared catalysts were characterized by XRD, N₂ adsorption-desorption, NH₃-TPD, FT-IR, SEM, and TEM techniques, and their catalytic performance was investigated in alkylation of toluene with tert-butanol. The adsorption capacity and the acid sites amount of HM/MCM-48-4 sample prepared by growing MCM-48 on the surface of HM zeolite are much higher than that of their mechanical mixture (HM/MCM-48(4) sample) due to its biporous structure; it shows higher catalytic performance than other HM/MCM-48 samples. The influence of reaction conditions on the catalytic performance of HM/MCM-48-4 zeolite was discussed. Toluene conversion of 41.4% and p-tert-butyltoluene selectivity of 73.5% were obtained at the weight ratio of toluene to HM/MCM-48-4 of 5, reaction temperature of 453 K, reaction time of 5 h and the molar ratio of toluene to tert-butanol of 0.5.     

Co掺杂ZnO/MCM-41分子筛的制备及对异戊醇的催化氧化性能

以Co掺杂的介孔分子筛MCM-41为载体, 采用等体积浸渍法制备了系列5%ZnO/xCo-MCM-41催化剂, 并用于催化分子氧氧化异戊醇合成异戊醛的反应. 通过X射线衍射(XRD), 傅里叶变换红外光谱(FTIR), 紫外-可见漫反射光谱(UV-Vis DRS), 扫描电子显微镜(SEM), 氨气程序升温脱附(NH₃-TPD), 氢气程序升温还原(H₂-TPR)和氮气吸附-脱附等手段对样品进行表征, 并考察了Co掺杂量对分子筛结构和催化性能的影响. 结果表明, 随着Co掺杂量的增大, 样品的比表面积和孔体积均减小, 而其平均孔径呈先增大后减小的趋势. 当Co掺杂量为0.05时, 5%ZnO/0.05Co-MCM-41仍保持了MCM-41高度有序的六方介孔结构, 具有高比表面积(989 m²/g)、较大孔径(2.88 nm)和孔体积(0.88 cm³/g), 引入的Co主要以孤立态钴离子[Single-site Co(Ⅱ)]形式存在于MCM-41骨架, MCM-41骨架中的Co可以有效提高ZnO微粒的分散度, 适度降低5%ZnO/MCM-41的表面酸性, 并大幅度提高5%ZnO/MCM-41的氧化还原性. 与5%ZnO/MCM-41相比, 5%ZnO/0.05Co-MCM-41可使异戊醛的选择性提高28.3%.