氨基功能化介孔氧化硅纳米中空球负载乙酰丙酮氧钒催化苯甲硫醚选择性氧化反应

首次将乙酰丙酮氧钒固载在氨基功能化的介孔氧化硅纳米中空球以及SBA-15(直型孔道结构)和SBA-16(笼型孔道结构)上,并应用于苯甲硫醚选择氧化反应.结果表明,在温和的反应条件下,上述催化剂均可催化苯甲硫醚高选择性地转化为亚砜产物(选择性最高大于99.0%).动力学对比实验表明,相比于直型和笼型介孔氧化硅,纳米中空球负载的催化剂具有更高的转化频率.这是因为纳米空心球尺寸小,更有利于催化活性中心的暴露以及反应物和产物在催化过程中的扩散.催化剂可循环使用多次,其活性和选择性基本保持不变.     

负载于孔道内部的手性酸碱催化不对称Aldol反应

将手性的伯胺-叔胺与B酸组成的酸碱对负载到介孔材料SBA-15孔道的内表面,得到了一种非均相双功能催化剂.该催化剂在催化丙酮和不同醛的aldol反应时得到了中等的活性和对映体选择性,重复使用6次后活性没有明显下降.与以硅胶为载体的催化剂相比,以介孔SBA-15分子筛为载体的催化剂ee值更高,这可能是由于介孔孔道限制效应引起的.     

氧化硅负载的固体碱上乙醛的气相缩合反应

在氧化硅负载的含碱金属固体碱催化剂上乙醛能有效地缩合生成丁烯醛及丁烯醇,反应具有中等转化率、较好的选择性(约90％)和稳定性.考察了不同反应条件对催化性能的影响,并对可能的反应活性相进行了探讨.     

介孔Ru-PPh2-KIT-6催化剂应用于水相中烯丙醇异构化的研究

以2-(二苯基膦)乙基三乙氧基硅烷和正硅酸乙酯为混合硅源,运用延时共缩聚法制备带有二苯基膦(PPh2-)修饰配体的KIT-6型介孔氧化硅材料,通过络合Ru(II)获得固载化Ru(II)有机金属催化剂(Ru-PPh2-KIT-6),该催化剂具有规整介孔结构.在水相烯丙醇异构化反应中显示高活性和高选择性,催化性能接近均相催化剂,活性相与载体结合牢固,能够重复使用5次以上.     

金复合介孔SBA-15吸附血红蛋白在H2O2电催化反应中的应用

以P123嵌段共聚物表面活性剂为模板剂制备介孔氧化硅SBA-15,并用沉积-沉淀(DP)法在SBA-15介孔表面负载纳米Au颗粒制备得到金复合介孔SBA-15材料(Au-SBA-15).再以Au-SBA-15材料制备玻碳修饰电极,将血红蛋白固定于修饰电极上用循环伏安法考察其对不同浓度H2O2溶液的电催化反应.在固定了血红蛋白的Hb/Au-SBA-15/GC修饰电极上,H2O2在+0.95 V处出现了氧化峰,且随着H2O2浓度的增大峰电流不断增加,说明金复合介孔氧化硅材料具有良好的生物兼容性,有利于血红蛋白的固定,其修饰电极对H2O2溶液具有一定的电催化作用.     

MCM-41 负载席夫碱催化α,β-不饱和酮的环氧化反应研究

介孔分子筛MCM-41 依次与3-氯丙基三乙氧基硅烷、环己二胺和三唑醛反应, 得到席夫碱修饰的新型介孔分子筛MCM-41 催化剂. 通过傅里叶变换红外光谱(FTIR)和X 射线多晶衍射(XRD)等方法对所得催化剂进行表征. 以过氧化氢为氧源, 介孔分子筛MCM-41 负载的席夫碱为催化剂, 研究了α,β-不饱和酮的环氧化反应, 考察了金属盐、溶剂、催化剂用量、反应时间等因素对环氧化反应的影响. 结果表明, 在室温下乙腈溶剂中, α,β-不饱和酮的环氧化反应在短时间内均以很高的产率(高达99%)得到了相应的产物. 同时, 对催化剂的重复利用进行了研究, 发现重复使用四次, 仍能以较高产率得到环氧化产物.     

介孔硅材料及其负载型催化剂去除挥发性有机物的最新进展

介孔硅材料由于具有大的比表面积,均一的孔结构和大的孔径,常被用于分离、吸附和催化等领域.本文综述了近年来国内外介孔硅材料及其负载型催化剂去除各类挥发性有机物(VOCs)的研究进展,主要包括烃类、甲醇、甲醛、丙酮、苯、甲苯、萘、乙酸乙酯等.讨论了介孔硅材料的结构对VOCs吸附过程的影响;介绍了不同催化剂消除各类VOCs的催化性能及反应机理,并重点评述了甲苯在不同催化剂上的研究进展.分析结果表明,介孔硅材料的表面环境、孔道结构以及宏观形貌是影响VOCs分子在介孔硅材料上吸附的主要因素;贵金属催化剂的应用需要提高其抗中毒性以及降低成本;过渡金属的研究应着重于研发高活性的负载型过渡金属复合氧化物催化剂.最后对国内外介孔硅材料及其负载型催化剂的发展进行了展望,今后催化剂的设计可以从“氧化硅载体”和“介孔孔道”两个方面展开,这将为设计合适的催化剂处理各类VOCs污染物提供一定参考.     

CO2 气氛下 MCF 负载氧化钒催化剂上乙苯脱氢反应

 以介孔氧化硅泡沫 MCF 为载体合成了一系列负载型氧化钒催化剂 (V 含量为 2%?10%). 采用 N2 吸附、X 射线衍射和 H2 程序升温还原对 V/MCF 催化剂的结构和织构性质进行了表征, 并评价了催化剂在 CO2 气氛下的乙苯脱氢性能. V/MCF 催化剂具有较高的乙苯脱氢活性, 其中 V 含量为 6% 的催化剂具有最高的反应活性. V/MCF 催化剂的乙苯脱氢活性显著高于 V/MCM-41, 这是由于前者具有较高的可还原性以及较好的扩散性能. CO2 气氛下的乙苯转化率明显高于 N2 气氛下的, 这归因于 CO2 与乙苯发生氧化脱氢, 并通过逆水煤气变换反应在线除去脱氢反应生成的氢.     

金复合介孔SBA-15吸附血红蛋白在H2O2电催化反应中的应用

以P123嵌段共聚物表面活性剂为模板剂制备介孔氧化硅SBA-15,并用沉积-沉淀(DP)法在SBA-15介孔表面负载纳米Au颗粒制备得到金复合介孔SBA-15材料(Au-SBA-15).再以Au-SBA-15材料制备玻碳修饰电极,将血红蛋白固定于修饰电极上用循环伏安法考察其对不同浓度H₂O₂溶液的电催化反应.在固定了血红蛋白的Hb/Au-SBA-15/GC修饰电极上,H₂O₂在+0.95 V处出现了氧化峰,且随着H₂O₂浓度的增大峰电流不断增加,说明金复合介孔氧化硅材料具有良好的生物兼容性,有利于血红蛋白的固定,其修饰电极对H₂O₂溶液具有一定的电催化作用.     

负载TS-1导向剂的介孔材料的合成、表征及催化性能研究

利用浸渍法将TS-1导向剂高度分散在介孔材料MCM-41和SBA-15的表面,制备出一系列在氧化反应中具有高活性的催化材料.对样品的表征显示催化剂保持了介孔的结构,同时具有四配位的钛物种均匀地分散于介孔催化剂的表面.催化结果显示,与钛硅分子筛(TS-1)相比,所制备的催化剂在小分子的氧化反应中表现出相似的活性,在大分子的氧化反应中展示了很高的活性,体现了介孔材料的优越性.     

周期有序介孔Rh(Ⅰ)有机金属催化剂用于水介质Heck反应的研究

以1,4-双(三乙氧基硅基)苯和2-(二苯基膦)乙基三乙氧基硅烷为混合硅源, 在表面活性剂作用下共缩聚得到二苯基膦功能化的有序介孔有机硅材料[PPh₂-PMO(Ph)], 通过配位作用将Rh(Ⅰ)有机金属催化剂固载到PPh₂-PMO上得到Rh(Ⅰ)-PPh₂-PMO(Ph)非均相催化剂, 并采用FTIR, NMR, XRD, TEM和氮气吸附等手段对催化剂进行了表征. 考察了该催化剂在水介质Heck反应中的催化性能, 实验结果表明, 所制备的Rh(Ⅰ)-PPh₂-PMO(Ph)具有与均相催化剂Rh(PPh₃)₃Cl相当的催化活性, 这主要归因于催化剂的高比表面积、有序介孔结构有利于提高Rh(Ⅰ)活性位的分散度, 减少了传质阻力; 同时PMO构建形成的微环境增强了表面疏水性, 有利于反应底物的吸附和扩散. 此外, 催化剂重复使用多次后活性仍没有明显降低.     

有机-无机杂化L-Rh/SiO2氢甲酰化催化剂的研究Ⅰ.PPh3-Rh/SiO2的催化性能及表征

 利用有机-无机杂化的概念,以三苯基膦直接修饰Rh/SiO2制备了PPh3-Rh/SiO2多相催化剂. 在浆态床烯烃氢甲酰化反应中,该催化剂在10 MPa,373 K温和条件下的活性和选择性远高于Rh/SiO2的活性和选择性,与相应的均相催化剂HRhCO(PPh3)3的性能相当,且具有易分离的优点. 31P MAS NMR和XPS技术表征结果表明,催化剂中的配体PPh3与高度分散的Rh之间存在配位作用,形成了兼具多相和均相催化性能的有机-无机杂化催化剂. 该催化剂对不同碳数烯烃的氢甲酰化反应都具有较好的催化性能.     

Direct Immobilization of Phosphine-Rhodium Complex on MCM-41 for Propene Hydroformylation

IntroductionHeterogenization of HRh( CO) ( PPh3 ) 3 ( PPh3 :triphenylphosphine) for hydroformylation andselective hydrogenation has received considerableattention in the past several decades from bothacademic and industrial interests[1] . Besides themilestone preparation of water- soluble TPPTS andthe corresponding rhodium- phosphine complexessuch as HRh( CO) ( TPPTS) 3 ( 1 ) [2 ,3 ] ,supportedliquid- phase catalysts ( SLPC) [4— 6] and supportedaqueous- phase catalysts ( SAPC) [7]…     

Ruthenium Carbenes Supported on Mesoporous Silicas as Highly Active and Selective Hybrid Catalysts for Olefin Metathesis Reactions under Continuous Flow

In the search for a highly active and selective heterogenized metathesis catalyst, we systematically varied the pore geometry and size of various silica‐based mesoporous (i.e., MCM‐41, MCM‐48, and SBA‐15) and microporous (ZSM‐5 and MWW) versus macroporous materials (D11‐10 and Aerosil 200), besides other process parameters (temperature, dilution, and mean residence time). The activity and, especially, selectivity of such “linker‐free” supports for ruthenium metathesis catalysts were evaluated in the cyclodimerization of cis‐cyclooctene to form 1,9‐cyclohexadecadiene, a valuable intermediate in the flavor and fragrance industry. The optimized material showed not only exceptionally high selectivity to the valuable product, but also turned out to be a truly heterogeneous catalyst with superior activity relative to the unsupported homogeneous complex.     

Gas diffusion and microstructural properties of ordered mesoporous silica fibers

Pore and surface diffusion of carbon dioxide (CO(2)) and ethylene (C(2)H(4)) in the nanopores of ordered mesoporous silica fibers about 200 microm in length was measured by the transient gravimetric method. The experimentally determined pore diffusivity data, coupled with the porosity, pore size, and fiber length, are used to obtain the actual length of the nanopores in silica fibers. These measurements reveal a structure of the ordered nanopores whirling helically around the fiber axis with a spiral diameter of about 15 microm and a pitch value of 1.6 microm. At room temperature the surface diffusion contributes about 10% to the total diffusional flux for these two gases in the nanopores of the ordered mesoporous silica fibers. The surface diffusion coefficients for the ordered mesoporous silica fibers are about 1 order of magnitude larger than the non-ordered mesoporous alumina or silica with similar pore size.     

Polymerization of 3‐ethynylthiophene with homogeneous and heterogeneous Rh catalysts

3‐Ethynylthiophene (3ETh) was polymerized with Rh(I) complexes: [Rh(cod)acac], [Rh(nbd)acac], [Rh(cod)Cl]₂, and [Rh(nbd)Cl]₂ (cod is η²:η²‐cycloocta‐1,5‐diene and nbd η²:η²‐norborna‐2,5‐diene), used as homogeneous catalysts and with the last two complexes anchored on mesoporous polybenzimidazole (PBI) beads: [Rh(cod)Cl]₂/PBI and [Rh(nbd)Cl]₂/PBI used as heterogeneous catalysts. All tested catalyst systems give high‐cis poly(3ETh). In situ NMR study of homogeneous polymerizations induced with [Rh(cod)acac] and [Rh(nbd)acac] complexes has revealed: (i) a transformation of acac ligands into free acetylacetone (Hacac) occurring since the early stage of polymerization, which suggests that this reaction is part of the initiation, (ii) that the initiation is rather slow in both of these polymerization systems, and (iii) a release of cod ligand from [Rh(cod)acac] complex but no release of nbd ligand from [Rh(nbd)acac] complex during the polymerization. The stability of diene ligand binding to Rh‐atom in [Rh(diene)acac] catalysts remarkably affects only the molecular weight but not the yield of poly(3ETh). The heterogeneous catalyst systems also provide high‐cis poly(3ETh), which is of very low contamination with catalyst residues since a leaching of anchored Rh complexes is negligible. The course of heterogeneous polymerizations is somewhat affected by limitations arising from the diffusion of monomer inside catalyst beads. © 2008 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 46: 2776–2787, 2008     

Cobalt(II) acetylacetonate complex immobilized on aminosilane‐modified SBA‐15 as an efficient catalyst for epoxidation of trans‐stilbene with molecular oxygen

From environmental and economic points of view, it is highly desirable to develop a clean and efficient catalytic process to produce epoxides. An attractive approach is to use a solid, recyclable catalyst and molecular oxygen as the oxidant without any sacrificial reductant or other additives. Nonetheless, the catalysts reported up to now still cannot balance catalytic activity with epoxide selectivity. It is of great importance to explore novel catalysts with both high activity and selectivity for the epoxidation of olefins. In this work, cobalt(II) acetylacetonate (Co(acac)₂) was covalently bonded to the silica surface of SBA‐15 molecular sieve by multi‐step grafting using 3‐aminopropytrimethoxysilane (APTS) as coupling agent. Characterizations with nitrogen physisorption, X‐ray diffraction, transmission electron microscopy, Fourier transform infrared spectroscopy and thermogravimetric analysis suggested that the metal complex was successfully immobilized on the aminosilane‐modified SBA‐15 surface and the channel structure remained intact. The synthesized Co(acac)₂APTS@SBA‐15 catalyst was used in the epoxidation of trans‐stilbene (TS) with molecular oxygen. Compared to the sample prepared by the impregnation method as well as Co(acac)₂ solutions under the same reaction conditions, the Co(acac)₂ immobilized catalyst exhibited remarkably higher TS conversion and trans‐stilbene oxide (TSO) selectivity. An increase in TS conversion with Co content was observed when the Co loading was lower than 0.70% and the 0.70Co(acac)₂APTS@SBA‐15 sample exhibited the best catalytic performance. Up to 50.1% of TS conversion could be achieved within 6 h, affording TSO selectivity as high as 96.7%. The superior catalytic performance of this particular catalyst is attributed to the high activity of the immobilized Co(acac)₂ species on SBA‐15. Copyright © 2016 John Wiley & Sons, Ltd.     

Polymerization of cyclohexene oxide with Al(acac)3-silanol catalyst supported by zeolite and porous silica

The polymerization of cyclohexene oxide with Al(acac)₃-silanol catalyst supported by zeolite and porous silica has been investigated. Cyclohexene oxide was also polymerized to a lesser extent by a zeolite-silanol catalyst and an Al(acac)₃-silica gel catalyst. The catalytic activity of the zeolite-silanol system varied with the zeolite pore size. The catalytic activity of the Al(acac)₃-silanol system was enhanced by supporting the catalyst with porous silica or zeolite. The Al(acac)₃-silanol catalyst supported by zeolite was especially effective in increasing polymer conversion and molecular weight. Catalytic activity increased with increasing chemical interaction between silanol and porous silica. The molecular weight of the polymers with these catalysts increased in the order zeolite-silanol> zeolite-Al(acac)₃-silanol >Al(acac)₃-silanol ≈ Al(acac)₃-silanol supported by porous silica>Al(acac)₃-silica gel.     

Highly regio- and stereoselective hydrothiolation of acetylenes with thiols catalyzed by a well-defined supported Rh complex

Highly regio- and stereoselective hydrothiolation of a wide range of alkynes with various thiols was demonstrated in the presence of a well-defined Rh complex supported on mesoporous SBA-15 silica. The catalyst was easily recovered and reused several times without significant loss of activity or selectivity.