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.     

二次嫁接法合成多金属氧酸盐/介孔分子筛杂化材料

合成了表面含有SiOH基团的钨磷酸盐衍生物(Bu4N)3PW11O39[O(SiOH)2] (TBAPW11Si2), 并通过其与纯硅介孔分子筛SBA-15表面SiOH的缩合反应, 将TBAPW11Si2二次嫁接到SBA-15的介孔孔道中, 得到了TBAPW11Si2/SBA-15介孔杂化材料. 表征结果显示, 孔内TBAPW11Si2的Keggin结构保留完整, 并与孔壁共价键联. 样品仍保持六方对称的孔阵结构, 但孔道部分被堵, 孔容、孔径、比表面积下降. 该杂化样品对甲基橙的光催化降解不仅显示高催化活性, 而且由于键联的多金属氧酸盐在水溶液中的抗浸取能力强, 催化剂的使用寿命大大延长.     

Nafion功能化介孔催化剂上苯甲醚/苯甲酰氯酰基化反应研究

苯甲醚/苯甲酰氯的酰基化产物4-甲氧基二苯甲酮是多种精细化工产品的重要中间体.本工作主要介绍了Nafion负载型SBA-15,SBA-16及Me-SBA-15介孔超强酸催化剂的制备及其在苯甲醚/苯甲酰氯酰基化反应中的应用.实验结果表明,单位时间单位Nafion活性位上的苯甲酰氯转化数高于传统HBeta沸石和硫酸氧化锆,且载量的增加能显著提高酰基化催化性能.甲基修饰的Me-SBA-15介孔材料明显改善了催化剂表面的疏水性能,有效减缓了多聚芳烃副产物的生成,反应的转化率得到大幅提高.相对一维孔道结构的介孔SBA-15而言,三维笼状结构的SBA-16对反应物及产物分子具有更好的扩散性能,该结构优势由酰基化反应的高初始活性得以充分体现.在整个反应过程中,该类催化剂对4-甲氧基二苯甲酮具有专一的选择性.     

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.     

Cu-Zn-Zr/SBA-15介孔催化剂的制备及CO2加氢合成甲醇的催化性能

以具有骨架结构的SBA-15介孔分子筛为载体,采用浸渍法合成了具有高比表面积、不同金属氧化物含量的Cu-Zn-Zr介孔催化剂CZZx/SBA-15(x=0.3,0.4,0.5,0.6).采用N2吸附-脱附(BET)、X射线衍射(XRD)、H2程序升温还原(H2-TPR)、CO2吸附(CO2-TPD)和透射电子显微镜(TEM)等手段对样品进行了表征.在固定床反应器上评价了其CO2加氢合成甲醇的催化性能.实验结果表明,CZZx/SBA-15催化剂具有介孔结构,负载的Cu O,Zn O和Zr O2能够很好地分散在表面,并且负载氧化物晶粒尺寸不同.催化剂的铜比表面积SCu与甲醇催化活性呈近似线性关系,其中CZZ0.4/SBA-15催化剂表现出最大甲醇选择性(54.32%),与CZZ相比,甲醇选择性增加24.85%.随着金属氧化物负载量的增大,催化剂比表面积和SCu明显减小,甲醇选择性与收率也相应减小,负载型CZZx/SBA-15催化剂表面结构对CO2加氢合成甲醇反应活性起关键作用.     

新型有机-无机杂化碱性介孔材料的合成——空间位阻对催化性能的影响

通过直接合成方法制备了2个二级胺功能化的SBA-15型有机-无机杂化碱性介孔材料.粉末X射线衍射分析、氮气吸附-脱附和透射电镜表征表明,合成的材料保持了SBA-15的有序介孔孔道结构,而热重、红外光谱和元素分析表明有机功能团被成功引入.在对硝基苯甲醛和丙酮的羟醛缩合反应中,相对于一级胺功能化的材料,二级胺功能化的SBA-15展示了极大改进的催化活性,这可能是由于具有更大空间位阻效应的有机功能团的引入导致了碱性胺中心催化活性增强.     

含钨SBA-15介孔分子筛催化剂的表面酸性和羟基分布

分别以浸渍法和水热晶化法制备了SBA-15介孔分子筛孔中插入氧化钨和碳化钨的催化剂,采用NH3-TPD测定了表面酸性和总酸量,并采用FT-IR研究了它们的表面羟基分布情况.NH3-TPD结果表明,浸渍法制备的含氧化钨的SBA-15介孔分子筛催化剂表面只有SBA-15介孔分子筛的弱酸位,而含碳化钨的SBA-15介孔分子筛催化剂表面还出现了W2C的强酸位.水热晶化法制备的含氧化钨的SBA-15介孔分子筛催化剂表面SBA-15介孔分子筛的弱酸位随W含量的增大略有增强, W含量较高时还出现了钨物种的强酸位;含碳化钨的SBA-15介孔分子筛催化剂表面除了SBA-15介孔分子筛的弱酸位外, W含量较低时有W2C的强酸位, W含量较高时有W2C和WC两种强酸位.傅里叶变换红外光谱结果表明,浸渍法和水热晶化法制备的含氧化钨和碳化钨的SBA-15介孔分子筛催化剂除表面自由硅羟基外,还存在着α, β和γ三种不同类型的氢键羟基,并且氢键羟基和催化剂的制备方法以及催化剂的W含量都有一定的关系.     

SBA-15固载脯氨酸催化剂的制备及其在不对称Mannich反应中的应用

以4-羟基-L-脯氨酸为原料合成了脯氨酸衍生物,并将其固载于介孔SBA-15分子筛上制备了Pro/SBA-15催化剂.用X射线衍射、N2吸附-脱附、扫描电镜和红外光谱等手段对Pro/SBA-15催化剂进行了表征,并考察了催化剂在不对称Mannich反应中的催化性能.结果表明,固载脯氨酸不影响SBA-15的有序介孔结构,只是其孔径、孔体积和BET比表面积有所减小,在不对称Mannich反应中具有较高的催化活性和对映选择性.与均相催化相比,以对硝基苯甲醛为反应物时可得到较高的分离收率(80%)和中等的对映选择性(ee=60%).催化剂通过简单分离后可重复使用4次以上,其催化性能基本保持不变.     

Nb-P/SBA-15催化剂的制备及其对果糖水解制5-羟甲基糠醛的催化性能

果糖催化脱水制5-羟甲基糠醛（5-HMF）是生物质转化制高附加值化合物过程中的一个重要反应。采用自制的介孔SBA-15,浸渍法制备了Nb/SBA-15催化剂,再经磷酸化处理制得Nb-P/SBA-15催化剂,研究了该催化剂在果糖脱水制5-HMF反应中的性能。SEM、TEM、BET和XRD表征结果表明,Nb/SBA-15和Nb-P/SBA-15完好地保留了SBA-15的微观结构,其内孔道直径为10 nm,铌酸在孔内表面分布均匀;负载铌和磷酸化后,孔壁变薄。NH₃-TPD结果显示,Nb/SBA-15经磷酸预处理后,不仅弱酸性位有所增加,而且产生了中强酸和强酸性位,使得在含水两相体系果糖脱水反应中,Nb-P/SBA-15比Nb/SBA-15具有更高的催化活性和5-HMF选择性。同时考察了反应温度、溶剂比例、反应时间对果糖脱水的影响,结果表明,以水/MIBK（V/V=1/2）为溶剂时,160 ℃下反应1.5 h,果糖转化率和5-HMF收率分别高达96.1%和92.6%。Nb-P/SBA-15经循环使用四次后仍具有较好的催化活性,表明该催化剂具有较高的耐水稳定性。     

巯基功能化介孔材料高效锚定钯负载型催化剂的制备及其苯酚加氢催化性能

以含巯基官能团有机硅烷修饰的介孔材料MCM-41和SBA-15为载体, 采用浸渍-氢气还原法制备了高分散和高活性的负载型Pd催化剂. X射线衍射、N₂吸附-脱附和透射电子显微镜表征结果显示, 所制Pd催化剂Pd-SH-MCM-41和Pd-SH-SBA-15具有很好的长程有序结构、分布均匀的孔径、高比表面积及高度分散的Pd颗粒. 苯酚加氢反应结果表明, 以Pd-SH-MCM-41和Pd-SH-SBA-15为催化剂时, 在80℃, 1.0MPa反应1h, 苯酚转化率达99%以上, 环己酮选择性为98%. 它们的催化活性为商业Pd/C催化剂的5倍, Pd/MCM-41和Pd/SBA-15催化剂的3倍. 这可归因于介孔材料表面修饰的巯基官能团对Pd的锚定作用, 避免了Pd颗粒的团聚, 使其高度分散在介孔材料上.     

Mesoporous SBA-15 materials modified with PW or W active species as catalysts for the epoxidation of olefins with H<Subscript>2</Subscript>O<Subscript>2</Subscript>

Five catalysts containing PW or W active species that anchored onto aminosilylated mesoporous silica SBA-15 by a post-grafting route were prepared and the resulting PW or W/APTES/SBA-15 hybrid materials were characterized by XRD, N₂ adsorption/desorption, surface area analysis, TEM, FT-IR, and ICP (inductively coupled plasma atomic emission spectroscopy). The names of these catalysts have been abbreviated as SBA-15m-a, SBA-15m-b, SBA-15m-c, SBA-15m-d, and SBA-15m-e according to the different active species. The PW or W active species were highly dispersed in the channels of the modified mesoporous materials. The interaction between PW or W species and amino groups grafted on the channel surface of SBA-15 led to the immobilization of PW or W species. Their catalytic activity in the epoxidation of cyclooctene with H₂O₂ as oxidant was investigated. Among them, SBA-15m-a showed the best performance, with 98.9% conversion and 98.4% selectivity. The catalyst could be reused for six times with a little decrease in activity.     

Reductive amination of cyclohexanol/cyclohexanone to cyclohexylamine using SBA-15 supported copper catalysts

Amination of cyclohexanol was investigated in vapour phase over copper catalysts supported on mesoporous SBA-15. The different products identified during reductive amination of cyclohexanol reaction were cyclohexanone, cyclohexylamine, along with small amounts of N-Cyclohexylidinecyclohexylamine and dicyclohexylamine. Among several catalysts tested for the reductive amination, 5% Cu supported on SBA-15 exhibited better catalytic performance than other catalysts with 36% selectivity towards cylclohexylamine at 80% cyclohexanol conversion. The optimum reaction conditions employed to achieve the best catalyst performance were at 250 °C, 0.1 MPa of H₂/NH₃, TOS-10h. The active Cu sites, acidity of the catalyst, and effect of reaction parameters play a pivotal role in the reductive amination reaction. The prepared catalysts were characterized by XRD, BET, SEM, H₂-TPR and NH₃-TPD. The dispersion of Cu, particle size, and metal surface area (m²/g) calculated from pulse N₂O decomposition method. TPR findings reveal the presence of substantially dispersed copper oxide species at lower loadings which is easily reducible than the bulk copper oxide species found at higher Cu loadings. The acidity measurements by NH₃-TPD analysis suggest that the maximum acidic strength was obtained at 5 wt% copper on porous SBA-15, and decreased with Cu loadings. The catalytic properties are well in agreement with the findings of catalysts characterization.     

Mesoporous SBA-15 materials modified with oxodiperoxo tungsten complexes as efficient catalysts for the epoxidation of olefins with hydrogen peroxide

A hybrid mesoporous SBA-15 material (2a) containing an oxodiperoxo tungsten complex of the type [WO(O₂)₂L] (L = pyrazolylpyridine) was synthesized by a post-grafting route. The organic–inorganic hybrid catalyst was characterized by means of XRD, N₂ adsorption–desorption and FT-IR. The catalytic property of 2a in the epoxidation of cyclooctene with H₂O₂ as the oxidant was investigated in comparison with other three kinds of hybrid tungsten containing SBA-15 materials bearing ethylenediamine, imidazole or 4,4′-bipyridine ligands. It was found that all oxodiperoxo tungsten catalysts were active at the reaction temperature of 55 °C with CH₃CN as solvent. However, only the catalyst with the pyrazolylpyridine ligand showed good recoverability and relatively high stability against leaching of active tungsten species. Moreover, this catalyst showed very high efficiency for H₂O₂ utilization, and its catalytic activity could be further improved by using solvent mixtures of CH₃CN and CH₃COOH.     

Metallic nickel supported on mesoporous silica as catalyst for hydrodeoxygenation: effect of pore size and structure

Catalytic hydrodeoxygenation (HDO) of anisole, a methoxy-rich lignin-derived bio-oil model compound, was carried out over a series of Ni-containing (5, 10, 20, and 30 wt%) catalysts with commercial silica and ordered mesoporous silica SBA-15 as support. Both supports and catalysts were characterized by N₂ adsorption–desorption isotherms, X-ray diffraction, CO chemisorption, and transmission electron microscopy (TEM). Catalytic reaction was performed at 250 °C and 10 bar H₂ pressure. Depending on the catalyst support used and the content of active metal, the catalytic activity and product distribution changed drastically. Increase of the nickel loading resulted in increased anisole conversion and C₆ hydrocarbon (benzene and cyclohexane) yield. However, loading more Ni than 20 wt% resulted in a decrease of both conversion and C₆ yield due to agglomeration of Ni particles. In addition, Ni/SBA-15 samples exhibited much stronger catalytic activity and selectivity toward C₆ hydrocarbon products compared with Ni/silica catalysts. The differences in catalytic activity among these catalysts can be attributed to the effect of the pore size and pore structure of mesoporous SBA-15. SBA-15 can accommodate more Ni species inside channels than conventional silica due to its high pore volume with uniform pore structure, leading to high HDO catalytic activity.     

Hydrophobic Modification of Pd/SiO2@Single‐Site Mesoporous Silicas by Triethoxyfluorosilane: Enhanced Catalytic Activity and Selectivity for One‐Pot Oxidation

To enhance the catalytic activity in a selective one‐pot oxidation using in‐situ generated H₂O₂, a hydrophobically modified core–shell catalyst was synthesized by means of a simple silylation reaction using the fluorine‐containing silylation agent triethoxyfluorosilane (TEFS, SiF(OEt)₃). The catalyst consisted of a Pd‐supported silica nanosphere and a mesoporous silica shell containing isolated Ti^IV and F ions bonded with silicon (Si?F bond). Structural analyses using XRD and N₂ adsorption–desorption suggested that the mesoporous structure and large surface area of the mesoporous shells were retained even after the modification. During the one‐pot oxidation of sulfide, catalytic activity was enhanced significantly by increasing the amount of fluorine in the shell. A hydrophobic surface enhanced adsorption of the hydrophobic reactant into the mesopore, while the less hydrophobic oxygenated products efficiently diffused into the outside of the shell, which improved the catalytic activity and selectivity. In addition, the present methodology can be used to enhance the catalytic activity and selectivity in the one‐pot oxidation of cyclohexane by using an Fe‐based core–shell catalytic system.     

Effect of the order of Ni and Ce addition in SBA-15 on the activity in dry reforming of methane

Dry reforming of methane has been carried out on SBA-15 catalysts containing 5 wt% Ni and 6 wt% Ce. The effect of the order of Ni and Ce impregnation on the catalytic activity has been studied. Both metals were added using the “two-solvent” method that favors metal dispersion inside the pores. Characterizations by XRD (low and high angles), N₂ sorption, SEM and TEM of the materials after metal addition and calcination indicate good preservation of the porosities and high NiO and CeO₂ dispersion inside the porous channels. Reduction was carried out before the catalytic tests and followed by TPR measurements. The most active reduced catalyst was the Ni–Ce/SBA-15 sample prepared by impregnating cerium first, then nickel. All catalysts were highly active and selective towards H₂ and CO at atmospheric pressure. Full CH₄ conversion was obtained below 650 °C. The higher performances compared to those reported in the literature for mesoporous silica with supported Ni and Ce catalysts are discussed.     

SBA-15负载的Cu(Ⅱ)席夫碱配合物催化的苯乙烯氧化反应制备苯甲醛

采用一步法将原硅酸四乙酯与3-氨丙基三乙氧基硅烷在表面活性剂P123作用下,酸性共水解制备出氨基功能化的介孔分子筛SBA-15(NH2-SBA-15),再利用其中氨基与水杨醛的缩合反应制备SBA-15固载的席夫碱,该席夫碱与Cu(NO3)2溶液反应最终制成固定于SBA-15的Cu(II)席夫碱配合物多相催化剂Cu-SBA-15.采用X射线衍射、红外光谱仪、紫外可见分光光度计、场发射电镜、透射电镜、N2吸附-脱附、元素分析、原子发射光谱和热重分析对催化剂进行了表征,并将此催化剂用于无有机溶剂条件下催化氧化苯乙烯制备苯甲醛,考察了反应时间、反应温度、H2O2用量、水的用量、催化剂用量对反应的影响.当反应温度为100°C,反应时间8 h,H2O2与苯乙烯的摩尔比为2:1,不额外添加溶剂,且催化剂用量为3.8 wt%时,苯乙烯的转化率最高为84.4%,苯甲醛选择性为83.9%,催化剂的TOF值为261.1 h–1,并且重复使用3次后活性没有明显下降.规则的孔道、较大的比表面积以及分布均匀的活性中心可能是催化剂活性提高的原因.     

金属改性SBA-15应用于乙醇水蒸气重整制氢的研究

采用水热法将Ce金属引入SBA-15骨架，合成一系列Ce-SBA-15（Si/Ce=40，20，10）载体，再通过浸渍法制得Co/Ce-SBA-15催化剂.利用XRD、UV-Vis、FT-IR、H₂-TPR、N₂吸附-脱附等手段对催化剂进行表征，并用于乙醇水蒸汽重整制氢反应（ESR），考察载体骨架中Ce金属对催化剂结构和性能的影响.结果表明，水热法制备可使得Ce离子进入到SBA-15分子筛骨架，合成的载体仍保持SBA-15特有的介孔结构.与Co/SBA-15催化剂相比，基于铈的储放氧功能，Ce的加入提高了活性金属分散度，降低了反应积碳的生成，改善了催化剂稳定性.适量铈与钴的协同作用，提高了钴物种的分散度，降低了钴的烧结程度，催化剂Co/Ce-SBA-15（Si/Ce=20）具有良好的催化活性，乙醇转化率为96.6%，H₂选择性达到75.5%，反应后积碳率仅为5.6%.     

Pd/PAMAM(聚酰胺-胺)/SBA-15催化剂的制备及催化性能

利用聚酰胺-胺型(PAMAM)树形分子为模板制备出粒径可控的Pd纳米颗粒(Pd DEN),然后通过超声波法制备了SBA-15分子筛负载的Pd/PAMAM复合材料(Pd SDEN)。XRD和TEM测试表明,负载后Pd纳米颗粒的粒径没有变化,且均匀分布在分子筛的孔道中,SBA-15分子筛的结构也没有变化。以对硝基苯酚还原为例,测试了Pd SDEN的催化性能,与Pd DEN相比,其具有更高的催化效率,重复使用5次后仍具有较好的催化活性,反应速率仅下降4%,且Pd/PAMAM复合材料仍能稳定存在于分子筛的孔道中。     

Preparation, Characterization and Catalytic Performance of La-SO4/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.