负载型金催化剂

介绍了负载型金催化剂的制备，吸附及催化性能，反应机理及活性中心结构的研究进展，展望了金催化剂的应用前景，提出了尚待深入研究的基础理论问题。     

配位聚合载体化催化剂ESR研究进展

本文概述了配位聚合载体化催化剂的ESR研究进展,介绍了载体研究、活性中心研究及计算机模拟技术研究方面的发展概况.     

加氢处理催化剂中钨的结构与其硫化性能研究

利用ＸＰＳ,高压连续流动反应器和化学处理等技术,考察了ＷＯ３／γ－Ａｌ２Ｏ３催化剂中加入ＮｉＯ和ＳｉＯ２对钨的结构状态及其硫化性能的影响。结果表明：金属钨在载体上存在两种状态：一种是与载体表面弱活性中心结合的钨易被硫化;另一种是与载体表面强活怀中心结合的钨四面体）,难被硫化;两种结合状态的比值约为６：４,加入ＮｉＯ或在γ－Ａｌ２Ｏ３     

负载型钯催化剂的硫中毒机理—硫对催化剂上CO吸附性质的影响

制备了负载型Pd/Al_2O_3和Pd/MgO催化剂,借助于CO探针分子,用原位FT-IR研究了不同状态的硫对催化剂上活性组分的影响,结果表明,吸附在多位活性中心上的硫(一般是不可逆吸附硫)除了屏蔽本身所在的活性点外,对周围单活性中心还具有电子效应;吸附在单活性中心上的硫(主要为可逆吸附硫),主要以屏蔽效应影响催化剂的性质,载体上的硫对活性组分的电子状态具有一定的影响。     

茂锆载体催化剂下的乙烯／辛烯共聚及聚合物的^13C NMR研究

茂锆载体催化剂下的乙烯／辛烯共聚及聚合物的~（１３）ＣＮＭＲ研究刘胜生，于广谦，黄葆同（中国科学院长春应用化学研究所长春１３００２２）关键词茂锆载体催化剂，共聚，序列分布，~（１３）ＣＮＭＲ由于茂锆催化剂具有高活性，单一活性中心等特点［１，２］，并且能...     

负载型烯烃聚合催化剂合成的新方法

介绍了负载型烯烃聚合催化剂合成的新方法,探讨了不同载体负载的Ziegler- Natta催化剂各组分之间的相互作用机理及活性中心的形成途径。对负载茂金属催 化剂的新型载体及新的负载方法进行了评述。     

V／Sb催化剂上丙烷氨氧化反应机理的Monte Carlo模拟

本文应用Ｍｏｎｔｅ Ｃａｒｌｏ方法对丙烷氨氧化的反应机理进行了初步研究。首先在分析了Ｖ／Ｓｂ金红石构催化剂的各个晶面之后，以１００面为模板建立了Ｖ／Ｓｂ双活性中心模型。在此基础上，对丙烷，氨及氧的不同进料摩尔比率对丙烯腈，丙烯及ＣＯＸ三种产物的影响规律进行了详细考察。     

异相Ziegler—Natta催化剂聚合机理若干研究进展

简述综述了异相Ｚｉｅｇｌｅｒ－Ｎａｔｔａ催化剂聚合机理若干研究进展，主要包括催化剂多活性中心，各活性中心的动力学参数的测定及给电子体的作用等。     

EXAFS研究合成甲醇催化剂Cu／ZnO／MxOy

有关CO。＋H。合成甲醇催化剂的研究已有许多报道［‘－’j，但目前对活性中心及反应机理的认识仍不～致，其中对活性中心的看法归纳起来有3种：（1）Cll为活性中心“‘；（2）Cll”为活性中心［’j；（3）Cll－CtJ”为活性中心［‘1．研究发现，第三组分（如AI刀。）的加入可防止Cu粒子的烧结［’］，使Cu产生无序及缺陷结构，有利于CO。的吸附、活化［‘j及起到高分散Cu／Zno的稳定剂的作用［’j．由于三组分催化剂结构的多相性和准非晶态性，通常的XRD方法难以明确了解其结构，而EXAFS方法对研究局部有序结构特别有效．本文以Z…     

层状粘土负载的金催化剂制备及其常温催化氧化活性

为了研究粘土的性质对其负载的金催化剂在CO常温氧化反应中的催化活性的影响,将金溶胶分别负载到类水滑石(LDHs)和经过壳聚糖改性的蒙脱石(CS-MMT)表面,得到纳米金颗粒呈高度分散状态的金催化剂样品.通过XRD、XRF、TEM、XPS等手段表征了金催化剂样品的物相、金的含量、金颗粒的粒径分布及金的存在价态,测试了催化剂样品对CO的常温转化率.结果表明:Au0是粘土负载的金催化剂对CO常温氧化反应的主要活性物种,碱性载体LDHs负载的金催化剂样品1.83%Au/Mg Al-CO32--LDHs表面只检测到Au0,金颗粒的平均粒径为2.6 nm,对CO的常温转化率能够达到100%,而酸性载体CS-MMT负载的金催化剂样品1.71%Au/CS-MMT表面同时存在氧化态和金属态的金,且Auδ+/Au0=1.1,金颗粒的平均粒径为2.1 nm,对CO的常温转化率仅为25%.     

Preparation and catalytic behaviour of sub-nanometer gold deposited on TiO2 by vacuum calcination

Titania-supported gold catalysts calcined under vacuum have been studied using a combination of TEM and activity measurements for CO oxidation. A time dependent study by TEM suggested the presence of highly dispersed gold, a high percentage of which lies below the 1 nm resolution limit. A comparison between Au/TiO₂ samples calcined in vacuum and air has shown large differences in catalytic behaviour, indicating that not only the size of gold particles but also the oxidized state of the support surface is important.     

Gold catalysts for pure hydrogen production in the water-gas shift reaction: activity, structure and reaction mechanism

The production of hydrogen containing very low levels of carbon monoxide for use in polymer electrolyte fuel cells requires the development of catalysts that show very high activity at low temperatures where the equilibrium for the removal of carbon monoxide using the water-gas shift reaction is favourable. It has been claimed that oxide-supported gold catalysts have the required high activity but there is considerable uncertainty in the literature about the feasibility of using these catalysts under real conditions. By comparing the activity of gold catalysts with that of platinum catalysts it is shown that well-prepared gold catalysts are significantly more active than the corresponding platinum catalysts. However, the method of preparation and pre-treatment of the gold catalysts is critical and activity variations of several orders of magnitude can be observed depending on the methods chosen. It is shown that an intimate contact between gold and the oxide support is important and any preparative procedure that does not generate such an interaction, or any subsequent treatment that can destroy such an interaction, may result in catalysts with low activity. The oxidation state and structure of active gold catalysts for the water-gas shift reaction is shown to comprise gold primarily in a zerovalent metallic state but in intimate contact with the support. This close contact between small metallic gold particles and the support may result in the "atoms" at the point of contact having a net charge (most probably cationic) but the high activity is associated with the presence of metallic gold. Both in situ XPS and XANES appear unequivocal on this point and this conclusion is consistent with similar measurements on gold catalysts even when used for CO oxidation. In situ EXAFS measurements under water gas shift conditions show that the active form of gold is a small gold cluster in intimate contact with the oxide support. The importance of the gold/oxide interface is indicated but the possible role of special sites (e.g., edge sites) on the gold clusters cannot be excluded. These may be important for CO oxidation but the fact that water has to be activated in the water gas shift reaction may point towards a more dominant role for the interfacial sites. The mechanism of the water gas shift reaction on gold and other low temperature catalysts has been widely investigated but little agreement exists. However, it is shown that a single "universal" model is consistent with much of the experimental literature. In this, it is proposed that the dominant surface intermediate is a function of reaction conditions. For example, as the temperature is increased the dominant species changes from a carbonate or carboxylate species, to a formate species and eventually at high temperatures to a mechanism that is characteristic of a redox process. Similar changes in the dominant intermediate are observed with changes in the gas composition. Overall, it is shown that reported variations in the kinetics, structure and reaction mechanism for the water gas shift reaction on gold catalysts can now be understood and rationalised.     

Interaction between metallic gold and support and its influence on catalysis

The interaction between gold particles and support in Au/TiO₂ and Au/Al₂O₃ catalysts prepared by immobilizing colloidal gold on the support was evidenced by X-ray photoelectron spectroscopy. The reducibility of the support is more responsible than the interaction between the nanogold particles and support for the activity of catalysts.     

CO combustion on supported gold clusters.

Recent progress in the understanding of the fascinating catalysis of CO combustion by supported gold particles is summarized. Focusing on size-selected gold clusters consisting of only a few atoms, that is, the size regime with properties nonscalable from the bulk properties, we discuss the current knowledge of the different factors controlling the reactivity at the molecular level. These factors include the role of the oxide support, its defects, cluster charging as well as the structural fluxionality of clusters, the cluster size dependency, and the promotional effect of water. By combining experimental results with quantum mechanical ab initio calculations, a detailed picture of the reaction mechanism emerges. While similar mechanisms might be active for gold nanoparticles in the scalable size regime, it is shown that for different systems (defined by the cluster size, the support, experimental conditions, etc.) the reaction mechanism differs and, hence, no generalized explanation for the catalytic driving force of small gold particles can be given.     

具有良好热稳定性的Al2O3改性Fe2O3基金催化剂

通过共沉淀法和沉积-沉淀法制备出了具有良好热稳定性的Al2O3改性Fe2O3基金催化剂, 并通过透射电镜(TEM)、X射线衍射(XRD)、N2吸附-脱附及热重和差示扫描量热(TG-DSC)分析等表征手段对催化剂的结构与表面形貌进行了研究分析. TEM测试结果表明: 500 ℃焙烧后, 未掺杂Al2O3的催化剂中金颗粒粒径分布较宽, 平均粒径约为7.0 nm, 载体颗粒尺寸在50-100 nm范围内; 而掺杂Al2O3的催化剂中金颗粒粒径分布变窄, 平均粒径约为5.0 nm, 且载体颗粒大小也明显小于未掺杂Al2O3的催化剂, 保持在30-50 nm的范围内. N2吸附-脱附测试结果表明, Al2O3的掺杂有利于保持催化剂的介孔结构和比表面积, 从而提高了载体的热稳定性. XRD和TG-DSC测试结果表明, Al2O3的掺杂可以有效地抑制Fe2O3的结晶, 进而抑制了高温焙烧过程中金颗粒的长大. 选用CO低温氧化反应对催化剂的活性进行了评价, 即使在500 ℃高温下焙烧12 h, 掺杂了Al2O3的催化剂仍然可在26.7 ℃将CO完全转化, 而未掺杂Al2O3的催化剂CO最低完全转化温度(T100)高达61.6 ℃. Al2O3的掺杂显著提高了催化剂的热稳定性能.     

Electrodeposition of gold particles on aluminum substrates containing copper

Electrodeposition of adhesive metal films on aluminum is traditionally preceded by the zincate process, which activates the aluminum surface. This paper presents an alternative approach for activation of aluminum by using films containing 99.5% aluminum and 0.5% copper. Aluminum/copper films are made amenable for subsequent electrodeposition by anodization followed by chemical etching of aluminum oxide. The electrodeposition of gold is monitored with electrochemical impedance spectroscopy (EIS). Analysis of EIS data suggests that electrodeposition of gold increases the interfacial capacitance from values typical for electrodes with thin oxide layers to values typical for metal electrodes. Scanning electron microscopy examination of aluminum/copper films following gold electrodeposition shows the presence of gold particles with densities of 10(5)-10(7) particles cm(-2). The relative standard deviation of mean particle diameters is approximately 25%. Evaluation of the micrographs suggests that the electrodeposition occurs by instantaneous nucleation followed by growth of three-dimensional semispherical particles. The gold particles, which are electrically connected to the conductive aluminum/copper film, support a reversible faradaic process for a soluble redox couple. The deposited gold particles are suitable for subsequent metallization of aluminum and fabrication of particle-type films with interesting catalytic, electrical, and optical properties.     

Synthesis,Characterization and Self-assembly of Gold-coated Iron Nanoparticles

Due to their small size (1-100 nm), nanoparticles exhibit novel materials properties that differ considerably from those of the bulk solid state. Especially in recent years, the interests in nanometer-scale magnetic particles are growing based on their potential application as high density magnetic storage media. A unique reverse micelle method has been developed to prepare gold-coated iron nanoparticles. XRD, UV/vis, TEM and magnetic measurements are used to characterize the nanocomposites. XRD only gives FCC paterns of gold for the obtained nanoparticles. There is a red shift and broadening of Au@Fe colloid relative to pure gold colloid in the absorption spectra. TEM results show that the average size of Au@Fe nanoparticle is about 10 nm. These nanoparticles self-assembled into wires in micron level under a 0.5 T magnetic field. Magnetic measurements show that the particles are superparamagnetic with a blocking temperature of 42 K. Coercivity of the obtained nanoparticles decreases with the measuring temperature, which are 730 Oe,320 Oe and 0 at 2 K, 10 K and 300 K, respectively.     

The effect of ozone on plasmon absorption of gold hydrosols. Quasi-metal and metal nanoparticles

The character of the interaction between ultrasmall gold nanoparticles and ozone is shown to be mainly governed by the particle structure. For borohydride sols of gold nanoparticles with sizes of ??3 nm, which are characterized by metallic properties, this interaction is reduced to reversible adsorption of ozone on their surface. At the same time, ozone adsorption on ??nonplasmon?? Au particles that have a diameter of 2 nm and a very defective structure results in their irreversible structural rearrangement and transition to a metallic state, which is accompanied by the appearance of a surface plasmon resonance. The set of the results obtained shows that nanoparticles of borohydride gold sols are more efficient as possible hemosensors of ozone than are larger particles synthesized by the citrate method.     

Chiral N-isobutyryl-cysteine protected gold nanoparticles: preparation, size selection, and optical activity in the UV-vis and infrared

We have prepared gold nanoparticles covered with N-isobutyryl-l-cysteine and N-isobutyryl-d-cysteine, respectively. These particles with a mean particle size smaller than 2 nm are highly soluble in water and are amenable to chiroptical techniques such as vibrational circular dichroism (VCD) and circular dichroism (CD) spectroscopy. Density functional theory shows that the VCD spectra are sensitive toward the conformation of the adsorbed thiol. Based on the comparison between the experimental VCD spectrum and the calculated VCD spectra for different conformers, a preferential conformation of the thiol adsorbed on the gold particles can be proposed. In this conformation the carboxylate group interacts with the gold particle in addition to the sulfur. The particles could furthermore be separated according to their charge and size into well-defined compounds. The optical absorption spectra revealed a well-quantized electronic structure and a systematic red-shift of the absorption onset with increasing gold core size, which was manifested in a color change with particle size. Some compounds showed basically identical absorption spectra as analogous gold particles protected with l-glutathione. This shows that these particles have identical core sizes (10-12, 15 and 18 gold atoms, respectively) and indicates that the number and arrangement of the adsorbed thiol are the same, independent of the two thiols, which have largely different sizes. Some separated compounds show strong optical activity with opposite sign when covered with the d- and l-enantiomer, respectively, of N-isobutyryl-cysteine. The origin of the optical activity in the metal-based transitions is discussed. The observations are consistent with a mechanism based on a chiral footprint on the metal core imparted by the adsorbed thiol.     

Support effect in high activity gold catalysts for CO oxidation

In this work, we present a detailed study concerning the evaluation of the metal-support interaction in high activity gold catalysts for CO oxidation. Using the colloidal deposition method, model catalysts were prepared, which allow the isolation of the effect of the support on the catalytic activity. Prefabricated gold particles were thus deposited on different support materials. Since the deposition process did not change the particle sizes of the gold particles, only the influence of the support could be studied. TiO2, Al2O3, ZrO2, and ZnO were used as support materials. Catalytic tests and high resolution transmission electron microscopy clearly show that the support contributes to the activity. However, our results are not in line with the distinction between active and passive supports based on the semiconducting properties of the oxidic material. The most active catalysts were obtained with TiO2 and Al2O3, while ZnO and ZrO2 gave substantially less active catalysts. Furthermore, the effect of other important parameters on the catalytic activity (i.e., particles size distribution, calcination temperature, and aging time for a Au/TiO2 catalyst) has also been studied. Using this preparation route, the catalysts show high-temperature stability, size dependent activity, and a very good long-term stability.