CoPc/MCM-41催化氧化环己烯合成环己烯酮

以MCM-41型介孔分子筛为载体,酞菁类金属大环配合物为活性组分合成出了CoPc/MCM-41型催化剂,并对其结构进行了表征。红外、XRD和热重分析证实,催化剂活性组分负载后其热稳定性明显增加。进而以自制的CoPc/MCM-41为催化剂,对分子氧氧化环己烯制备环己烯酮的工艺条件进行了探索,结果表明,在催化剂用量120 mg(5 mL环己烯),反应温度55℃,反应时间8 h,二氯乙烷为溶剂的条件下,环己烯酮的单程产率可达24.2%,催化剂可分离回收,回收催化剂重复使用5次后,活性下降约3%。     

含Ni介孔分子筛的合成及其对苯加氢催化性能

采用水热法合成出不含镍和含镍的硅基介孔分子筛.利用XRD、FT-IR、TPR、TEM和比表面孔径测定等手段对样品进行了表征.结果表明：合成出有序性好的介孔分子筛（MCM-41）,550 ℃焙烧可以将模板剂有效去除,所合成介孔分子筛负载Pt后介孔有序性降低,但是介孔结构仍然存在.苯催化加氢反应研究表明：不含Ni的介孔分子筛不具有加氢活性,当将其负载Pt后具有苯加氢催化活性;含Ni介孔分子筛本身具有苯加氢活性,含Ni介孔分子筛负载Pt后苯加氢催化活性有较大的提高,所有样品的环己烷选择性都接近100 %,说明含Ni介孔分子筛可以直接作为苯加氢反应的催化剂或作为苯加氢催化剂良好的载体.     

包覆型Hβ和MCM-41复合分子筛作载体制备Pt加氢脱硫催化剂的研究

以Hβ为内核、十六烷基三甲基溴化铵为模板剂、偏硅酸钠为硅源,采用附晶生长法在Hβ表面包覆了一层MCM-41介孔相。分别以Hβ、MCM-41、包覆型复合分子筛(βM)以及Hβ和MCM-41机械混合物(β+M)作载体,采用等体积浸渍法制备了Pt催化剂。以二苯并噻吩(DBT)为模型含硫化合物,考察了催化剂的加氢脱硫(HDS)反应性能。结果表明,引入酸性Hβ载体不同程度地提高了催化剂的HDS活性,但也加剧了HDS产物的裂化反应。Pt/βM的HDS活性与Pt/Hβ接近,显著高于Pt/MCM-41和Pt/β+M。DBT在Pt/MCM-41上以直接脱硫路径为主,且不发生裂化反应。Pt/βM兼具很高的HDS活性和较低的裂化选择性,同时预加氢路径选择性也有所提高,说明包覆型βM复合分子筛是一种潜在的优异深度HDS催化剂载体。     

负载型CTAB/MCM-41介孔分子筛的制备及其对溴代反应催化性能的研究

采用水热晶化法,以CTAB为模板剂合成出MCM-41介孔分子筛,后经过220℃低温焙烧4 h,可成功将CTAB固载于MCM-41,并对产物进行了XRD表征。将制备的CTAB/MCM-41催化剂用于1,7-庚二醇的溴代反应,通过对使用不同催化剂条件下反应速率的比较表明:CTAB/MCM-41的催化活性较好于未负载的CTAB。负载型的催化剂经多次使用后活性基本不变,并且能够简化反应后的分离步骤。     

硅基纳米材料结合阿司匹林的缓释作用研究

本文在碱性条件下,硅酸钠作为硅源,十六烷基三甲基溴化铵(CTAB)作为结构模板剂,利用水合晶化法合成了纯硅源的MCM-41介孔分子筛.采用浸渍法将阿司匹林组装在MCM-41六方形孔道中,制备出新型载药Aspirin/MCM-41复合物。采用X射线粉末衍射(XRD)和傅里叶红外光谱(FT-IR)表征手段对合成的新型功能化介孔材料进行表征。MCM-41分子筛与阿司匹林的相互作用为研发以MCM-41分子筛为载体的载药体系提供了理论依据。     

Mo-MCM-41催化环戊烯烯丙型氧化的研究

研究了负载钼MCM-41和MCM-48分子筛对环戊烯烯丙型氧化的催化性能。两种介孔材料中,2-环戊烯-1-酮均为主要产物,副产物是少量的环戊烯氧化物和1,2-环戊二醇。实验显示钼MCM-48由于含钼量较高,表现出比钼MCM-41更高的反应活性,使用极性溶剂(如N,N-二甲基甲酰胺和甲醇)2-环戊烯-1-酮选择性降低,极性溶剂诱发双键氧化,生成较多的环戊烯氧化物。钼基固体催化剂,MCM-41和MCM-48再循环使用,对2-环戊烯-1-酮的选择性几乎没有改变。     

MCM-41分子筛加氢裂化催化剂的研究

按水热法合成出介孔MCM-41分子筛，在不同的气氛下焙烧脱除有机模板剂。在固定床流动反应器上，与USY分子筛对比了正庚烷加氢裂化结果，发现MCM-41分子筛有较好的抗氮中毒能力，且其稳定时的加氢裂解活性比USY分子筛高。     

金属酞菁催化氧化含硫化合物的实验研究

采用浸渍法将1,4,8,11,15,18,22,25-(异戊氧基)酞菁钴(铜,镍)分别负载到介孔分子筛MCM-41上,形成MCM-41-Co Pc,MCM-41-Ni Pc,MCM-41-Cu Pc组装体。在(20±1)℃,p H=7氧气气氛下,以各组装体为催化剂,研究了其对Na2SO3溶液的催化氧化活性。实验结果表明:各组装体具有良好的催化氧化性能,不同金属酞菁组装体表现出不同的催化活性,MCM-41-Co Pc催化剂的催化氧化性能最好。同种催化剂在不同浓度Na2SO3溶液中的催化活性也有所不同,此类催化剂可重复利用5次。负载型金属酞菁对硫化物的催化氧化作用,可以应用到油气田开发中的污水处理方面,对环保贡献了一定力量。     

苯乙烯环氧化反应分子筛催化剂研究进展

综述了苯乙烯环氧化制取环氧苯乙烷的几种分子筛／H2O2催化体系，介绍了微孔分子筛（TS-1）、Ti-ZSM-5和Ti-ZSM-11分子筛介孔分子筛（MCM-41），β-钛硅分子筛、负载金属配合物的中孔分子筛及其在苯乙烯环氧化反应中的性能。     

Pd-MCM-41介孔材料的合成、表征及催化性能研究

用微波辐射法合成了介孔分子筛MCM-41,采用浸渍法获得不同钯含量的Pd-MCM-41催化剂,用XRD、低温N2吸附-脱附、IR对MCM-41及组装体进行了表征;研究了Pd负载量、反应时间、反应温度等条件对葡萄糖氧化反应的影响,结果表明Pd-MCM-41能有效催化葡萄糖氧化反应。     

Assemblies of Ti Active Sites Over HMS Supports Containing Surface's OH or NH2 Groups

Three types of HMS supports, which were as-synthesized, HMS(u), HMS(c) calcined from HMS(u), and HMS(m) prepared by the modification of HMS(c) with 3-amino propyltriethoxysilane, were first used to assemble the Ti catalytic sites through the exchange reactions between them and Ti compounds such as Ti tetraisoproxide (Ti(OⁱPr)₄), Ti tetrachloride (TiCl₄)) and their Ti tartrate complexes. The Ti-assembled HMS catalysts were investigated in detail by means of FT-IR, UV–vis reflection spectra, chemical and elemental analyses. It is found that in Ti(OⁱPr₄ and especially TiCl₄, the exchange that takes place with the surface hydroxyls of the HMS(c) is easier than with the surface NH₂ groups of HMS(u) and HMS(m). Ti tartrate complex can be successfully assembled on the HMS(c) through three assembled pathways. The UV–vis reflection spectra indicates that the Ti species are highly dispersed upon the surface of HMS. In catalyzing epoxidation of styrene with TBHP, the above-described catalysts show a higher catalytic activity and selectivity for the epoxides than unloading Ti tartrate complex, and the Ti-substituted HMS catalysts. Their outstanding advantage is that they can be reused many times with little loss of activity.     

Synthesis and investigation of anchored copper (II) complexes within MCM-41 as selective catalysts for epoxidation of olefins

In the present study, preparation, characterization and catalytic activity of encapsulated copper (II) complexes within MCM-41 were investigated. The mesoporous molecular sieve MCM-41 was synthesized and grafted with 3-(trimethoxysilyl)-1-propanethiol to give a thiol modified material (MCM-41-S). The prepared material successively was reacted with acrylic acid and acrylonitrile to give AA-MCM-41 and AN-MCM-41, respectively. Using hexamethyldisilazane and copper (II) chloride, copper (II) complexes in the cavities of MCM-41 (Cu-AA-MCM-41 and Cu-AN-MCM-41) were prepared. The presence of copper (II) complex on the surfaces of host matrix and the structure of prepared catalyst is investigated by FT-IR, inductively coupled plasma-optical emission spectroscopy (ICP-OES), powder X-ray diffraction (XRD) and BET nitrogen adsorption–desorption methods. The catalytic activities of the catalysts were studied in epoxidation of olefins. The results showed that activities of the prepared catalysts (Cu-AA-MCM-41 and Cu-AN-MCM-41) and their selectivity to corresponding epoxides were more than those of MCM-41. In addition, the synthesized heterogeneous catalysts were truly reusable.     

Synthesis, characterization of high Ti-containing Ti-MCM-41 catalysts and their activity evaluation in oxidation of cyclohexene and epoxidation of higher olefins

A series of titanium rich isomorphous substituted Ti MCM-41 and HMS materials have been synthesized with different Si/Ti ratios. The highest amount of Ti incorporated in synthesis gel is in TiMCM-41 (Si/Ti = 10). Whereas for TiHMS catalysts, Ti is incorporated up to Si/Ti = 50 successfully without forming any extra framework TiO₂. Cyclohexene epoxidation reaction with dry tert-butyl hydroperoxide (TBHP) as an oxidant has been studied to evaluate the catalytic properties of Ti substituted mesoporous catalysts. The effect of molar ratio of substrate:oxidant in this reaction has been studied and high conversion, high selectivity were achieved at 2: 1 molar ratio with TiMCM-41 (Si/Ti =25). Dry TBHP (in dichloromethane) and chloroform were found as good oxidant and solvent system for this reaction. Pure siliceous mesoporous silica and low `Ti' substituted mesoporous silicas were found to be efficient catalysts for oxidation of cyclohexene. An interesting variation of the selectivity from allylic oxidation to epoxidation during oxidation of cyclohexene was observed with an increase in the Ti amount in the mesoporous framework. The allylic oxidation of cyclohexene has been carried out using molecular oxygen as an oxidant and in the presence of a small amount of TBHP as initiator. Siliceous HMS materials gave better conversion compared to MCM-41 type of materials and other conventional silicas like silica gel, fumed silica etc. in allylic oxidation of cyclohexene. Epoxidation of higher cyclic olefins like cyclooctene, cyclododecene, cis-cyclododecene and linear olefins 1-Heptene, cis-2-hexene, 1-undecene was carried out over TiMCM-41 (Si/Ti = 25). Ti substituted mesoporous catalysts were characterized by elemental analysis, XRD, FTIR, UVDRS, ²⁹SiMASNMR, BET surface area and pore size distribution techniques.     

Synthesis, Characterization of Ag/MCM-41 and the Catalytic Performance for Liquid-phase Oxidation of Cyclohexane

Nano-scale silver supported mesoporous molecular sieve Ag/MCM-41 was directly prepared by one-pot synthesis method. The prepared sample was characterized by XRD, TEM, and N₂ sorption. The results showed that the sample of Ag/MCM-41 had no appreciable incorporation of silver into the mesoporous matrix of MCM-41 with good crystallinity, and silver nanoparticles were dispersed inside or outside of the channels in the mesoporous host. The catalytic performance of the sample for the cyclohexane liquid-phase oxidation into cyclohexanone and cyclohexanol by oxygen in the absence of solvents without inducing agents was investigated. The 83.4% selectivity to cyclohexanol and cyclohexanone at 10.7% conversion of cyclohexane was obtained over Ag/MCM-41 catalyst at 428 K for 3 h. The turn over numbers (TONs) of Ag/MCM-41 was up to 2946. The catalytic activity of Ag/MCM-41 was also compared with Ag/TS-1 as well as Ag/Al₂O₃. The results indicated that Ag/MCM-41 showed superior activity to both Ag/TS-1 and Ag/Al₂O₃. A calcined Ag/MCM-41 was found to be an efficient catalyst for the cyclohexane oxidation into cyclohexanol and cyclohexanone using oxygen as oxidant.     

Characterisation and catalytic properties of MCM-41 and Pd/MCM-41 materials

Pure silica MCM-41 mesoporous molecular sieve material was synthesised and characterised by in situ synchrotron XRD, TEM, TGA/DTA and DRIFTS techniques. In situ energy dispersive XRD (EDXRD) confirmed the exact nature of the pore diameter of MCM-41 and the change in crystal structure on calcination. The IR band at 1057 cm^-1 of as-synthesised MCM-41 was shifted by 14 cm^-1 on heating to 673 K due to increased condensation of silanol groups to form Si-O-Si bridges. Calcined MCM-41 materials were used to support Pd, and the catalytic activities for 1-hexene and benzene selective hydrogenation were investigated. The Pd/MCM-41 catalyst showed high activity in hydrogenation of 1-hexene at an inlet reaction temperature of 298 K, but did not show any activity in hydrogenation for benzene. TEM results for the reduced Pd/MCM-41 catalysts revealed that the average Pd particle size was around 2-2.5 nm and these particles were located in the pores of MCM-41 and showed good distribution. TPR measurements showed that about 70% of palladium oxide (PdO) loading in the calcined catalysts was reduced at sub-ambient temperature. This revised version was published online in July 2006 with corrections to the Cover Date.     

Ti-MCM-41分子筛催化剂的合成、表征及催化性能

以正硅酸四甲酯为硅源,钛酸四异丙酯为钛源,在异丙醇和水的混合溶液中室温下合成了Ti-MCM-41介孔分子筛,采用TEM、N 2吸附-脱附、XRD、UV-Vis和Raman等研究了分子筛的结构特性。并以过氧化氢异丙苯为氧化剂,考察了硅烷化处理后的Ti-MCM-41分子筛催化剂在丙烯环氧化反应中的催化性能。结果表明,与骨架外六配位钛物种相比,骨架内四配位钛物种活化有机过氧化物的能力更强,速率更快;四配位钛物种是环氧丙烷生成的活性物种,而六配位钛物种的存在则会导致反应副产物的生成。合成时添加适量的异丁醇可有效促进钛物种进入分子筛骨架中,并增大比表面积和孔体积,进而改善Ti-MCM-41催化剂的丙烯环氧化催化性能。性能最佳的催化剂上过氧化氢异丙苯转化率可达94.7%,环氧丙烷选择性可达95.8%。     

Alkynes Hydrogenation over Pd-Supported Catalysts

The liquid-phase stereoselective hydrogenation of phenyl alkyl acetylenics at 298 K and atmospheric pressure on Pd-supported catalysts has been studied. The catalysts were prepared by impregnation of Pd(acac)₂ precursor (1 wt% of Pd) on different siliceous substrates such as amorphous SiO₂, mesoporous MCM-41 and silylated MCM-41. The poisoning effect of lead incorporation on the supported palladium was also studied. All the catalysts displayed high selectivity to cis-alkene isomer, with Pd/MCM-41 being the most active catalyst. Deliberately adding lead to the base, palladium catalysts underwent changes in the selectivity to cis-alkene isomer and a significant drop in the activity. All the solids were characterized by nitrogen adsorption–desorption isotherms at 77 K, TGA, TPR, H₂ and CO chemisorption, XRD, XPS, and TEM.     

Synthesis, structural characterization and photocatalytic activity of Ti-MCM-41 mesoporous molecular sieves

This paper reports the applicability of hydrothermal synthesis in alkaline medium for preparation of Ti-containing mesoporous MCM-41 materials. The influence of different parameters was investigated, such as the Ti source, the molar ratio between Si and Ti and also the synthesis temperature. Structural analysis shows that the high specific surface area, large pore size and well ordered mesostructure, are partially retained in the titania containing materials. Modifying synthesis temperature, it was shown that MCM-41 isotherms are different for temperatures above or under 140°C. UV-VisDR spectroscopy was used to investigate the local environment of Ti sites. The obtained materials were evaluated for the photocatalytic degradation of Rhodamine 6G in aqueous medium. The best photocatalytic activity was found for the sample prepared at higher ageing temperature of 160°C, at which anatase particles were formed.     

Ti-containing MCM-41 catalysts for liquid phase oxidation of cyclohexene with aqueous H2O2 and tert-butyl hydroperoxide

Framework Ti-substituted and Ti-grafted MCM-41 mesoporous material has been prepared by direct hydrothermal synthesis and a post-synthesis grafting method. The materials have been tested as catalysts for cyclohexene oxidation with aqueous H₂O₂ and tert-butyl hydroperoxide (TBHP). With aqueous H₂O₂ in methanol, the major products were cyclohexene diol and its methyl ethers. No cyclohexene oxide was produced. Titanium leaching was a serious problem, and the catalyst lost its activity irreversibly after only one cycle of reaction. With TBHP, the selectivity for cyclohexene oxide was near 100%, titanium leaching was negligible, and the catalyst could be repeatedly used after regeneration without suffering significant activity loss. However, the reaction rate was lower than when H₂O₂ was used. Framework substituted material and catalysts prepared by Ti-grafting onto a MCM-41 support behaved similar, but the Ti-grafted MCM-41 is somewhat more active. The turnover frequency (TOF) per mole of Ti decreases with an increase of Ti content in the catalyst. This is caused by a reduced Ti dispersion within the silica matrix. This revised version was published online in July 2006 with corrections to the Cover Date.     

Catalytic activity of mesoporous catalysts in Friedel–Crafts benzylation of benzene

Different samples of metal-incorporated MCM-41 were prepared and used as catalysts in Friedel–Craft’s benzylation of benzene. The catalytic performance was evaluated by off-line GC analysis. Fe-MCM-41 exhibited excellent activity, the sample with Si/Fe ratio = 10 showed 90% conversion with 95% selectivity towards diphenylmethane within a few minutes. Generally, the activity per Fe-site was an order of magnitude higher for the samples containing a combination of Fe₂O₃ nano-particles and isolated Fe³⁺ sites. A synergy of two catalytic centers (particles and isolated sites) is proposed to explain the high performance of the highly loaded samples. The catalytic performance of Fe-MCM-41 was superior to other metal-containing MCM-41 (e.g. Ga, Sn, and Ti) catalysts, or other Fe-containing mesoporous materials (e.g. Fe-HMS).