Au/Ce1-xZrxO2催化剂的制备、表征及其在CO氧化和水煤气变换反应中的催化性能

采用共沉淀法制备了不同锆铈摩尔比的Ce1-xZrxO2(x=0,0.1,0.3,0.5,0.7,0.9和1.0)氧化物,并以改性的浸渍法制备了金担载量为1%(质量分数)的Au/Ce1-xZrxO2催化剂.考察了催化剂在低温CO氧化和水煤气变换反应中的催化性能.应用氮物理吸附、X射线衍射、透射电镜和H2程序升温还原等技术对氧化物载体及其负载金催化剂进行了表征,并与其催化性能进行了关联.结果表明,与纯CeO2和ZrO2相比,Ce1-xZrxO2的比表面积增大而孔径减小,孔分布更加集中.Zr的加入使表面Ce4 的还原更加困难,使体相Ce4 的还原更加容易.活性组分金的加入有利于铈锆氧化物的还原.ZrO2载体较大的孔径使金在载体表面分散均匀而粒子较小,因此与Au/CeO2和Au/Ce1-xZrxO2相比,Au/ZrO2具有更好的低温CO氧化活性和水煤气变换活性,而Au/CeZrO在高温下的水煤气变换反应中表现出更好的催化性能.     

水滑石负载 Au 纳米粒子的制备及其催化醇氧化反应

 采用离子交换法和 NaBH4 还原法制备了 Mg-Al-水滑石 (LDH) 负载的 Au 纳米粒子 (Au/LDH) 催化剂. X 射线衍射和透射电镜结果表明, Au 粒子较均匀地分散在水滑石表面, 载体仍保持层状结构. 在温和的反应条件下, Au/LDH 对一系列醇的氧化反应表现出优异的催化性能, 如在室温常压下进行分子 O2 氧化 1-苯基乙醇的反应, 底物转化率和苯乙酮选择性都接近 100%, 而且催化剂经过多次循环使用后, 其活性未见下降. 可见, Au/LDH 催化剂在醇氧化反应中具有良好的应用前景.     

金催化一氧化碳氧化反应中锌锡复合氧化物的载体效应

氧化物负载的纳米金催化剂对CO氧化反应具有极高的活性,这不仅依赖于金的结构特性,也取决于氧化物载体的结构.近年来,除了氧化硅、氧化铝等惰性载体以及氧化钛、氧化铈、氧化铁等可还原性载体外,人们还致力于探索各类新型氧化物载体.另一方面,锡酸锌是具有反尖晶石结构的化合物,并且在透明导电氧化物、锂离子电池阳极材料、光电转换装置以及传感器等方面应用广泛.然而,迄今为止,锡酸锌仍未被用于负载纳米金催化剂,因此相关的构效关系作用研究也十分有限.基于此,本文采用氮气吸附-脱附实验、电感耦合等离子体原子发射光谱(ICP-AES)、X射线衍射(XRD)、X射线光电子能谱(XPS)、透射电子显微镜(TEM)和高分辨电镜(HRTEM)、高角环形暗场像-扫描透射电子显微镜(HAADF-STEM)、X射线吸收精细结构谱(XAFS)和氢气程序升温脱附(H2-TPD)等手段,系统研究了锡酸锌负载的纳米金催化剂在CO氧化反应中催化性能差异的原因.首先,利用水热法制备了锡酸锌(ZTO)载体,而其织构性质可由碱(N2H4·H2O)与金属离子(Zn2+)的比例在4/1(ZTO_1)、8/1(ZTO_2)和16/1(ZTO_3)之间进行调节.结果发现, ZTO_2具有最大的孔体积(0.223 cm3/g)和最窄的孔径分布.再采用沉积沉淀法将0.7 wt% Au负载于其上,得到金-锡酸锌(Au_ZTO)催化剂. ICP-AES测得样品中Au含量在0.57-0.59 wt%,与投料比接近. CO氧化反应结果显示, Au_ZTO_1和Au_ZTO_2的表观活化能相同,但后者的活性更高;而Au_ZTO_3在220°C以下没有活性,催化性能最差,与纯锡酸锌载体相当. XRD结果显示,反应过程中ZTO晶相、晶胞参数及晶粒尺寸变化不明显; TEM和HRTEM分析表明,载体ZTO在反应前后均为多面体形貌,平均颗粒尺寸在12-16 nm; XPS结果验证了Zn2+和Sn4+离子是新鲜和反应后样品中载体金属的存在形式; HAADF-STEM探测到所有样品中均含有1-2 nm的Au粒子; XAFS结果表明, Au以Au0形式存在,并且在Au_ZTO_3中Au平均粒径大于4 nm,而其它两样品约为2 nm. H2-TPR结果表明,金的引入对ZTO载体耗氢量影响不大,但还原峰温度向低温移动;金属-载体相互作用强弱与催化活性高低具有正相关性,即Au_ZTO_2> Au_ZTO_1>> Au_ZTO_3.这是由于不同织构性质的锡酸锌载体对于纳米金活性物种的稳定作用不同所致,具有最大孔体积和最窄孔径分布的ZTO_2负载的金纳米颗粒表现出最高活性.     

SiO2负载Au-Pd双金属纳米颗粒催化甲醇选择性氧化合成甲酸甲酯

甲醇选择氧化制备甲酸甲酯（MF）是延伸甲醇产业链、开发高附加值下游产品的有效途径之一,负载型Au及Pd催化剂在这一反应中表现出优异的低温催化性能。为探索实用、高效和易再生的甲醇选择氧化催化剂,同时揭示双金属颗粒中Au和Pd的协同效应及甲醇氧化反应机理,本研究制备了一系列二氧化硅负载的Au-Pd催化剂（Au-Pd/SiO₂）,详细研究了其对甲醇选择氧化制甲酸甲酯的催化性能。结果表明,Au和Pd总负载量为0.6%、且Au/Pd质量比为2时,所制备的Au₂-Pd₁/SiO₂催化剂表现出优异的甲醇氧化催化性能;在130℃下,甲醇转化率达到57.0%,MF选择性为72.7%。多种表征结果显示,Au-Pd双金属纳米颗粒粒径为2-4 nm,高度分散于SiO₂载体表面,倾向于生成孪晶结构并暴露（111）晶面,这些因素是Au-Pd/SiO₂具有优异催化性能的主要原因。通过DRIFTS表征研究,提出了一个可能的MF生成机理：即甲醇首先与处于Au-Pd纳米粒子界面的表面氧作用,生成化学吸附的甲氧基;随后,甲氧基经去质子作用生成吸附的甲醛物种,后者与相邻的甲氧基物种亲核反应,并经β-H消除后得到目标产物MF。     

CuO—ZrO20—CeO2复合氧化物的催化性能研究

研究了氧化铜的加入对锆铈复合氧化物的结构与性能的影响,发现氧化铜的加入可降低氧化铈的还原温度,稳定复合氧化物的立方结构,提高对CO氧化的催化活性,增加铈含量能提高催化剂的活性,而硫酸盐等可使催化剂的活性降低,掺铜锆铈复合氧化物催化剂的活性几乎不受高温灼烧的影响,是一种具有较高热稳定性的催化剂。     

氧化锆负载氧化钌催化甲醇低温选择氧化合成甲酸甲酯的活性催化剂结构

 采用ZrO2负载的RuOx催化剂在低温(如373 K)下催化甲醇选择氧化合成甲酸甲酯,发现RuOx的结构可显著影响反应速率和产物选择性. 在相近的甲醇转化率下, RuO2-4物种的催化活性和对甲酸甲酯的选择性明显高于RuO2物种, 表明在ZrO2表面构筑高活性高选择性的RuO2-4结构有利于获得高的甲酸甲酯产率.     

Mn-Al和Cu-Mn-Al复合氧化物催化苯甲醇选择氧化反应

用溶胶-凝胶法制备了不同组成的Mn-Al和Cu-Mn-Al复合氧化物两组催化剂,用于苯甲醇选择氧化反应.用X射线衍射(XRD)、N2物理吸附(BET)、扫描电镜(SEM)、H_2程序升温还原(H_2-TPR)、O_2程序升温脱附(O_2-TPD)和X射线光电子能谱(XPS)技术对催化剂进行了结构表征,考察了催化剂组成对催化活性的影响.结果表明:以甲苯为溶剂,O_2为氧化剂,353 K反应5 h,Mn_2Al和Cu_(0.3)Mn_(0.7)Al_2催化剂上的苯甲醇转化率分别为36.6%和40.9%,苯甲醛选择性均为100%.进一步研究表明:催化剂活性与其H2还原性和O_2吸附性有关,高活性的催化剂吸附氧多,生成的活性氧易参与反应.     

富CO2气氛中镨基复合氧化物载金催化CO氧化反应

采用传统水热法制备了一系列不同镨锆摩尔比的镨锆复合氧化物PraZrbOx载体,并考查了富CO2气氛下相应Au/PraZrbOx催化剂催化CO氧化反应的催化性能。研究发现Pr/Zr=0.005为最优摩尔比,其对应的Au/Pr0.005Zr1Ox催化剂因较易吸附更多的氧分子而表现出最好的催化活性。结合XRD、CO2-TPD、TEM、XPS等表征手段发现：反应过程中活性物种Au的价态和氧物种组分含量发生变化,这一因素是造成催化剂活性差异的关键性因素。此外通过稳定性测试发现无论是Au/ZrO2还是Au/PraZr1Ox系列催化剂均不受高浓度CO2的影响。     

共沉淀法制备甲烷部分氧化制甲醇用多元复合氧化物催化剂

采用三种共沉淀工艺制备了甲烷部分氧化制甲醇用Ｍｏ－Ｃｒ－Ｖ－Ｂｉ－Ｓ多元复合氧化物催化剂，发现不同共沉淀工艺过程对催化剂体相中Ｍｏ，Ｃｒ，Ｖ，Ｂｉ的含量及催化剂的活性有一定影响。ＸＲＤ结果表明，与Ｃｒ相比，Ｂｉ与Ｖ及Ｍｏ之间有更强的结合能力。     

Insights into support effects on Ce-Zr-O mixed oxide-supported gold catalysts in CO oxidation

Au/Ce1xZrxO2 catalysts (x=0-0.8) were prepared by a deposition-precipitation method using Ce1xZrxO2 nanoparticles as supports with variable Ce and Zr contents. Their structures were characterized by complimentary means such as X-ray diffraction, Raman, scanning transmission electron microscopy and X-ray photoelectron spectroscopy (XPS). These Au catalysts possessed similar sizes and crystalline phases of Ce1xZrxO2 supports as well as similar sizes and oxidation states of Au nanoparticles. The oxidation state of Au nanoparticles was dominated by Au 0 especially in CO oxidation. Their activities were examined in CO oxidation at different temperatures in the range of 303 333 K. The CO oxidation rates normalized per Au atoms increased with the increasing Ce contents, and reached the maximum value over Au/CeO2. Such change was in parallel with the change in the oxygen storage capacity values, i.e. the amounts of active oxygen species on Au/Ce1xZrxO2 catalysts. The excellent correlation between the two properties of the catalysts suggests that the intrinsic support effects on the CO oxidation rates is related to the effects on the adsorption and activation of O2 on Au/Ce1xZrxO2 catalysts. Such understanding on the support effects may be useful for designing more active Au catalysts, for example, by tuning the redox properties of oxide supports.     

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.     

Selective oxidation of methanol on cuprate catalysts

The catalytic activity of BaCuO₂, Ba₂Cu₃O₅ and YBa₂Cu₃O_7–x has been compared in the selective oxidation of methanol to formaldehyde. Ba₂Cu₃O₅ shows the highest activity.

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BaCuO₂, Ba₂Cu₃O₅ YBa₂Cu₃O_7–x . Ba₂Cu₃O₅ .

     

Nanoparticle size effects on methanol electrochemical oxidation on carbon supported platinum catalysts

The particle size effect observed on the performance of Pt/C electrocatalysts toward the methanol oxidation reaction (MOR) has been investigated with differential electrochemical mass spectrometry (DEMS). The investigation has been conducted under both potentiodynamic and potentiostatic conditions as research on methanol electrochemical oxidation is closely related to interest in direct methanol fuel cells. The particle size effect observed on the MOR is commonly regarded as a reflection of different Pt-CO and Pt-OH bond strengths for different particle sizes. This work focuses mainly on the mechanism of methanol dehydrogenation on platinum which is central to the problem of the optimization of the efficiency of methanol electro-oxidation by favoring the CO(2) formation pathway. It was found that the partitioning of the methanol precursor among the end products on supported platinum nanoparticles is strongly dependent on particle size distribution. Also, it is postulated that the coupling among particles of different sizes via soluble products must be considered in order to understand the particle size effects on the observed trends of product formation. An optimum particle size range for efficiently electro-oxidizing methanol to CO(2) was found between 3 and 10 nm, and loss in efficiency is mostly related to the partial oxidation of methanol to formaldehyde on either too small or too large particles. The possible reasons for these observations are also discussed.     

Physico-chemical properties of iron-tin mixed oxide catalysts in cyclohexane oxidation

The state of mixed iron-tin oxide catalysts with a variable ratio of their metallic components has been studied by Mössbauer and ESCA spectroscopy. The results are compared with the activity of these catalysts in cyclohexane oxidation.

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Genesis of a highly active cerium oxide-supported gold catalyst for CO oxidation

X-Ray absorption spectra show that a CeO(2)-supported CO oxidation catalyst prepared from Au(III)(CH(3))(2)(C(5)H(7)O(2)) initially incorporated Au(III) complexes that were catalytically active at 353 K; during operation in a flow reactor, the gold aggregated into clusters and the catalytic activity increased.     

Steady state catalytic properties and oxygen binding energy of cadmium-molybdenum catalysts in methanol oxidation

On normal cadmium molybdate the products of methanol oxidation are primarily CO₂ and H₂. After the introduction of excess MoO₃ to reach Mo/Cd=1.2, methanol is oxidized to formaldehyde and carbon monoxide via a consecutive scheme. The oxygen binding energy in the steady state for the first sample is by 30 kcal/mol higher than that for the second catalyst. The activation energies of methanol conversion are 11.5 and 20 kcal/mol, respectively.

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CO₂ H₂. MoO₃ Mo/Cd=1, 2 . 1- 30 / , , , , 11,5 20 /.

     

Preferential oxidation of carbon monoxide on supported gold catalysts

Catalyst precursors containing 1% Au were synthesized by the impregnation of Al₂O₃ and CeO₂-Al₂O₃ supports with an aqueous solution of HAuCl₄ followed by drying, treatment with aqueous ammonia for the removal of chlorine residues, and final drying at 90°C. The oxidation of CO in gas containing ～1 vol % O₂, ～1 vol % CO, 60 vol % H₂, and the balance N₂ on the activated catalysts was studied. In a number of experiments, to 18 vol % water was added to the gas mixture. The activation of precursors by the initial gas was studied. It was found that the prolonged storage of a precursor in air made its activation difficult to perform. The 1%Au/Al₂O₃ catalyst activated by the gas mixture stably operated in the preferential oxidation of CO at room temperature with the occurrence of the reaction in the mode of catalyst surface ignition (a hot spot at the bed inlet) under a change in the feed gas flow rate by a factor of 3. The effect of the presence of additional CO₂ (to 39 vol %) on the oxidation of H₂ was studied: the catalyst activity decreased. Because the reaction of CO₂ reduction to CO did not occur, the effect can be due to the adsorption of CO₂ on gold. The effect of the addition of water vapor to the feed gas was studied with the use of 1%Au/CeO₂-Al₂O₃ as an example. The exo/endo effects related to the adsorption/desorption of water on the catalyst surface were detected upon steam supply and shutoff at a bed temperature of 100–150°C. It was noted that the addition of water vapor to a certain level favorably affected the selectivity (decreased the residual concentration of CO). The boundary water concentration, at which the effect became negative, depended on catalyst bed temperature. The higher was the bed temperature, the greater amount of water could be added until the manifestation of a negative effect.     

Variations in electronic state of silver catalysts for methanol oxidation

Variations in the electronic state of silver catalysts for methanol oxidation under the effect of the reaction medium have been studied, using diffuse reflectance spectroscopy. The nature of active centers-Ag⁺ cations, Ag _n ⁺ complexes and clusters of various sizes for bulk and supported catalysts are shown to be identical.

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. - Ag⁺, Ag _n ⁺ .

     

Electro-oxidation of methanol on platinum-organic metal complex mixed catalysts in acidic media

Novel mixed catalysts systems have been developed using a platinum tetraammine complex with a cobalt or nickel quinolyldiamine complex supported on graphite powder and heart treated at 600 degrees C in argon atmosphere, for the methanol oxidation reaction in direct methanol fuel cells.