Au/NTS-1催化丙烯气相直接环氧化(英文)

以高温氨气处理制得含氮微孔钛硅分子筛(NTS-1)为载体,用沉积-沉淀法制得了一系列纳米金催化剂.考察了纳米金催化剂在氢气和氧气共存下催化丙烯气相环氧化制环氧丙烷反应中的催化性能.结果表明,高温氨气处理钛硅分子筛(TS-1)载体降低了其酸性,提高了纳米金催化剂制备中金的利用率和纳米金催化剂中金的分散度,显著提高纳米金催化剂的催化活性.载体酸性降低和载体表面–NH2配位效应增强了催化剂活性.     

Au/CuxMnyOz催化剂的制备、表征及其CO消除性能

采用溶胶一凝胶法制各了新型CuxMnyOz:复合氧化物,并利用沉积-沉淀法制各了1%Au/CuxMnyOz:系列催化剂样品,在富H2条件下评价了该催化剂在CO选择性氧化反应和水煤气变换(WGS)反应中的催化性能,结果发现,极少量Au的负载使得CuxMnyOz复合氧化物不仅具有良好的CO氧化活性和选择性,而且在WGS反应...     

钛硅复合氧化物局域结构的研究

用XAFS（X-ray absorption fine structure）分析了由溶胶-凝胶、液相浸渍和化学气相沉积等三种方法制备的二氧化钛和二氧化硅复合氧化物的Ti K边结构.结果表明:溶胶-凝胶法制得的复合氯化物中的钛分散很好,液相浸渍法次之,而化学气相沉积法最差.不论哪种方法,随钛含量（或钛硅原子比）的增加,边前特征峰A2降低,钛的第一配位层Ti－O的配位数和键长增加;在复合载体中既有钛中心对称的八面体6配位TiO6的结构也有钛中心对称性差的四面体4配位TiO4或五面体5配位结构,并且随钛含量增加,钛的局域结构越来越接近锐钛矿型二氧化钛.根据XAFS、XRD、IR表征结果,提出了钛硅复合氧化物模型.     

Au/Ti-MCM-41(H)催化丙烯气相直接环氧化

采用纳米组装法制备了一系列不同Ti含量的具有微孔-介孔复合结构(hybrid)的钛硅分子筛Ti-MCM-41(H)载体,继而用沉积-沉淀法制得纳米金催化剂.通过粉末X射线衍射(XRD)、氮气等温吸附-脱附、傅里叶变换红外(FT-IR)光谱、紫外-可见漫反射(DRUV-Vis)光谱、透射电镜(TEM)及等离子体原子发射光谱法(ICP-AES)对催化剂进行了表征,并考察了纳米金催化剂在氢气/氧气共存条件下丙烯气相直接氧化制环氧丙烷反应中的催化性能.结果表明:合成的微孔-介孔复合结构的钛硅分子筛Ti-MCM-41(H)具有典型的MCM-41结构,Ti(IV)以高分散的形式存在于分子筛的骨架结构中.在常压、423K反应温度下,以Ti/Si摩尔比为1%的Ti-MCM-41(H)为载体制备纳米金催化剂表现出了最佳的催化性能,反应30min,丙烯的转化率达5.4%,环氧丙烷的选择性为74.2%,环氧丙烷的生成速率为73.1g·h-1·kg-1;反应330min后,丙烯的转化率为4.9%,环氧丙烷的选择性为67.3%.     

Au/MBFCN多组分复合型催化剂用于低温催化氧化丙烯制丙烯醛

钼铋系催化剂在丙烯氧化制丙烯醛反应中具有独特优势,但对反应温度、水汽配比的要求均较高。金催化剂的低温催化性能优异且对产物选择性高,我们结合二者的优势,通过调变载体制备过程中沉淀终止时的pH得到了一系列多组分复合氧化物担载金催化剂（Au/MBFCN）。反应结果显示,pH=4、载金量为0.5wt%时得到的催化剂Au/MBFCN-4性能较优,在水汽配比5vol%、反应温度300 ℃下,丙烯转化率可达22.9%,丙烯醛选择性为91.2%。用HRTEM、XRD、Raman和XPS等对催化剂进行表征,发现pH较低时得到的催化剂中MoO3、Bi2Mo3O12、Fe2(MoO4)3等活性晶相的含量较多,是Au/MBFCN-4低温催化性能优异的主要原因。     

非均相催化一步合成碳酸二苯酯的研究 I．载体制备方法对催化剂性能的影响

采用溶胶－凝胶法、共沉淀法和冷冻干燥法，制备了LaxMnyPbzO复合型氧化物载体，并以PbCl2或Na2PbCl4的水溶液为浸渍液，通过浸渍方法制固相催化剂，用于一步俣成碳酸二苯酯，用XRD，TEM及SEM对载体及催化剂进行了表征，结果表明，三种载体的主要物相皆为La0.3Mn0.5PbO，溶胶－凝胶法制得的载体及催化剂的粒径分布较好，空隙率较大，活性组分分散度较高；溶胶－凝胶法制得的催化剂的催化性能较好，碳酸二苯酯选择属于选择性可高于99．5％。     

La2O3助剂对Au/TiO2催化肉桂醛选择性加氢性能的影响

以溶胶-凝胶法制得的TiO2和La2O3-TiO2为载体,采用沉积-沉淀法制备了一系列Au催化剂,用于肉桂醛选择性加氢反应,并运用N2吸附-脱附、X射线衍射、高分辨率透射电镜、程序升温还原和X射线光电子能谱等方法对催化剂进行了表征,系统考察了La2O3含量对Au/TiO2催化剂物化性质和催化性能的影响.结果表明,适量L...     

溶胶-凝胶和浸渍-水热制备方法对TiO_2/AC光催化剂结构和性能的影响

分别采用溶胶-凝胶法和浸渍-水热法制得负载于活性炭(AC)的TiO2催化剂,并用扫描电镜(SEM)、X射线衍射(XRD)、拉曼光谱和氮气吸附等方法对催化剂进行了表征.结果表明:溶胶-凝胶法制得的TiO2以不规则碎片形式涂附在载体表面,而浸渍-水热法制得的球形TiO2颗粒呈柱形生长均匀覆盖在载体表面;不同温度处理的浸渍-水热法制得的TiO2/AC光催化剂的中孔和微孔比表面积均大于溶胶-凝胶法制得的样品,负载的TiO2粒径则小于溶胶-凝胶法制得的样品.对甲基橙(MO)溶液的光催化降解测试结果表明,600℃煅烧为两种方法的最佳热处理温度,浸渍-水热法制得的催化剂光催化效果明显强于溶胶-凝胶法的.     

Au/N-Ti-HMS的制备及其催化丙烯直接环氧化反应的研究

以十二胺为模板剂合成了一系列不同Ti含量的介孔分子筛Ti-HMS,并通过高温氨处理对其进行高温改性,在分子筛表面和骨架中引入碱性N原子.分别以改性前后的Ti-HMS为载体使用沉积沉淀法制得纳米金催化剂,并考察氢气、氧气共存条件下催化丙烯气相直接环氧化的催化性能.通过氮气等温吸附-脱附、X射线衍射(XRD)、傅里叶变换红...     

高热稳定性纳米Au/TiO2催化剂的制备与表征

 采用三嵌段共聚物聚乙醚-聚丙醚-聚乙醚EO20PO70EO20 (P123)为有机模板剂合成了介孔TiO2载体,用沉积-沉淀法制得Au/TiO2催化剂. 运用N2 吸附-脱附、 X射线衍射、 X射线光电子能谱和高分辨电镜技术对催化剂的结构与形貌进行了表征. 采用P123模板剂合成的TiO2具有较均匀的介孔结构,孔径集中在6.1 nm附近,负载金后,其介孔结构保持良好,但孔径下降至5.4 nm. 400 ℃焙烧后,介孔TiO2负载的Au催化剂中Au主要以金属态存在. 负载在三种TiO2载体(介孔TiO2、溶胶-凝胶法合成的TiO2和工业TiO2)上的Au晶粒大小和分散度差异较大,其中介孔TiO2载体更有利于金的分散,以该载体制备的催化剂400 ℃焙烧后金的晶粒尺寸在1～5 nm范围内,催化剂显示了很好的CO氧化活性和抗热稳定性,即使在420 ℃焙烧,其室温下CO的转化率也在90%以上. 而溶胶-凝胶法制备的TiO2和工业TiO2负载的纳米金催化剂中,金晶粒尺寸约为10 nm,催化剂的CO氧化活性和抗热稳定性较差.     

丙烯在Au/TiO2催化剂上的化学吸附与临氢环氧化反应

环氧丙烷;丙烯环氧化;丙烯在Au/TiO2催化剂上的化学吸附与临氢环氧化反应     

Direct gas-phase epoxidation of propylene to propylene oxide using air as oxidant on supported gold catalyst

Gold catalysts supported on SiO2, TiO2, TiO2-SiO2, and ZrO2-SiO2 supports were prepared by impregnating each support with a basic solution of tetrachloroauric acid. X-ray diffraction （XRD）, transmission electron microscopy （TEM）, and X-ray photoelectron spectroscopy （XPS） techniques were used to characterize their structure and surface composition. The results indicated that the size of gold particles could be controlled to below 10 nm by this method of preparation. Washing gold catalysts with water could markedly enhance the dispersion of metallic gold particles on the surface, but it could not completely remove the chloride ions left on the surface. The catalytic performance of direct vapor-phase epoxidation of propylene using air as an oxidant over these catalysts was evaluated at atmospheric pressure. The selectivity to propylene oxide （PO） was found to vary with reaction time on the stream. At the reaction conditions of atmosphere pressure, temperature 325 ℃, feed gas ratio V（C3H6）/V（O2）= 1/2, and GHSV =6000h^-1, 17.9% PO selectivity with 0.9% propylene conversion were obtained at initial 10 min for Au/SiO2 catalyst. After reacting 60 min only 8.9% PO selectivity were detected, but the propylene conversion rises to 1.4% and the main product is transferred to acrolein （72% selectivity）. Washing Au/TiO2-SiO2 and Aa/ZrO2-SiO2 samples with magnesium citrate solution could markedly enhance the activity and PO selectivity because smaller gold particles were obtained.     

Molecular approaches towards mixed metal oxides and their behaviour in mixed oxide support Au catalysts for CO oxidation

We herein report a water-based sol-gel approach towards porous mixed Si/Ti oxides using co-precipitated glycol-modified precursors. By adjusting synthesis parameters such as the pH value and the Si/Ti ratio of the precursor, the morphology as well as the Si/Ti-composition of the resulting mixed oxide particles can be varied in a wide range. The behaviour of the mixed oxides as substrates for Au catalysts and the performance of the resulting catalysts in the CO oxidation reaction was investigated and compared to catalysts supported on mesoporous anatase and rutile synthesized analogously. For comparable Au particle sizes and Au loadings, the composition of the mixed oxide support was found to significantly affect the reactivity and reaction behaviour, with mixed oxide supported Au catalysts synthesized at pH=5 or 10 and with a Si/Ti-ratio of 1:19 and 1:34 exhibiting the maximum activity. In contrast to the enhanced activity, the mixed oxide supports do not lead to a significant improvement in deactivation behaviour and catalyst stability.     

Study on Chemisorption, Catalytic Behavior, and Stability of Supported Au Catalyst for the Propylene Epoxidation Reaction

The supported Au/TiO2 and Au/TiO2-SiO2 catalysts were prepared by deposition precipitation method. The TPD study reveals that propylene oxide competes with propylene to be adsorbed on the same adsorptive center-Tin site on the surface of the catalyst and that the adsorbing capacity of the catalyst for propylene oxide is larger than that for propylene. Catalytic behavior for propylene epoxidation with H2 and O2 was tested in a micro-reactor. Under typical conditions, the selectivity for propylene oxide is over 87%. The TG curves show that PO successive oxidation cause carbon deposition on the active center and deactivation of the Au catalysts. Because the amounts of Tin site decrease significantly, and consequently the separation between Tin sites increases, the Au/TiO2-SiO2 catalyst is more stable than Au/TiO2.     

不同沉淀剂制备的Ag／TS－1催化丙烯直接气相氧化合成环氧丙烷

 在423K、常压固定床石英反应器中，以丙烯直接气相氧化为探针反应，考察了催化剂制备方法、沉淀剂的种类和浓度对制备的Ag／TS－1催化剂催化性能的影响，采用TEM，XRD和UV－Vis等表征手段对Ag／TS－1催化剂进行了分析．结果表明，沉积－沉淀法是最佳的催化剂制备方法，但浸渍法也可制得具有环氧丙烷选择性的催化剂．K2CO3是一种良好的沉淀剂．以K2CO3为沉淀剂，硅钛比为64的TS－1为载体制备的Ag／TS－1催化剂上的丙烯转化率为1．72％，环氧丙烷选择性为98．2％．少量单质银的存在有利于环氧丙烷的生成，除银粒子的分散状态外，银粒子与载体TS－1间的相互作用对提高催化剂的选择性具有决定性作用．     

丙烯环氧化制环氧丙烷Fe-Al-P-O催化剂的研究

用溶胶-凝胶法制得了Fe-Al-P-O催化剂，采用IR、XRD、TEM、BET、TPR和微反等技术研究了催化剂的物化性质和反应性能。实验结果表明，Fe1/2-Al1/2-PO4由10 nm左右 FePO4和AlPO4微晶组合而成，其晶格氧的活泼性大于单纯FePO4，AlPO4在Fe1/2-Al1/2-PO4中起到分散FePO4微晶的作用；Fe1/2-Al1/2-PO4的反应性能与原料气组成密切相关，丙烯与O2的选择氧化产物主要是丙烯醛，原料气中加入H2后，反应产物以环氧丙烷为主，同时还有部分丙烯醛，原料气中引入水蒸气后，可进一步增加环氧丙烷的选择性及减少丙烯醛的产率；在0.1 MPa、200 ℃、C3H6/O2/H2/H2O/N2=1∶1∶1∶1∶6（mol比）和空速1 200 h－1条件下，丙烯的转化率为8.9％，环氧丙烷的选择性为81.0％。     

A New Method for Preparing Ti-Si Mixed Oxides

Ti-Si mixed oxides with different TiO2 content were prepared by sol-gel one step hydrolysis, using TiCl4 as the precursor. The samples were characterized by BET, FT-IR and XRD. The results indicated that titanium is in fourfold coordination with oxygen in the SiO4^4- in mixed oxides, form the bond of Ti-O-Si, and the low titania materials are mixed on an atomic scale.The phase of anatase appeared when TiO2 content is up to 80%. The mixed oxides had high specific surface areas up to 681.5 m^2/g. 10TiSi is a better support than SiO2 in the reaction of CO oxidation.     

Non-hydrolytic sol-gel routes to heterogeneous catalysts

Oxides and mixed oxides have a tremendous importance in the field of heterogeneous catalysis, serving either as catalysts or as supports for active species. The performance of a catalyst depends directly on its composition, texture, structure and surface properties, which have to be precisely controlled and adapted to each application. In this context, the sol-gel process is a unique tool for the preparation and understanding of catalytic materials, owing to its exceptional versatility. In the last 10 years, the non-hydrolytic sol-gel (NHSG) or non-aqueous sol-gel process based on nonhydrolytic condensations in nonaqueous media has established itself as a simple and powerful method for the design of a wide range of oxide, mixed oxide and hybrid materials with controlled composition, morphology, texture and structure. NHSG proved particularly interesting for the preparation of catalytic materials, notably mesoporous xerogels, single site catalysts and highly crystalline nanoparticles. This critical review addresses the application of NHSG to the preparation of heterogeneous catalysts, emphasizing the specificities of this process, and giving a comprehensive overview of the literature (251 references).     

When gold is not noble: catalysis by nanoparticles

Bulk gold is chemically inert and is generally regarded as a poor catalyst. However, when gold is in very small particles with diameters below 10 nm and is deposited on metal oxides or activated carbon, it becomes surprisingly active, especially at low temperatures, for many reactions such as CO oxidation and propylene epoxidation. The catalytic performance of Au is defined by three major factors: contact structure, support selection, and particle size. The role of the perimeter interfaces of Au particles as the sites for reactions is discussed as well as the change in chemical reactivity of Au clusters composed of fewer than 300 atoms.