铈基复合氧化物的结构及其对HCl催化氧化性能的影响

采用氨水共沉淀法制备了一系列铈基复合氧化物(Ce0.9M0.1O2,M=Cu、Cr、Zr、Ti、La),借助XRD、Raman、N2吸附-脱附、ESEM和H2-TPR等手段对复合氧化物的结构进行了表征,并考察了其在HCl催化氧化制Cl2过程中的性能.结果显示:Cu、Cr和Zr掺杂能显著减小复合氧化物晶粒尺寸,提高复合氧化物的比表面积和孔容,并提供更多的低温可还原氧物种.而La和Ti的掺杂可以获得较大的表面氧空位浓度以及增加高温可还原氧物种数目.复合氧化物结构和表面性质的变化显著影响了其HCl催化氧化活性,在430℃下铈基复合氧化物催化剂活性顺序为:Ce0.9Cu0.1O2Ce0.9Cr0.1O2Ce0.9Zr0.1O2Ce0.9Ti0.1O2Ce O2Ce0.9La0.1O2,低温可还原氧物种数目直接与催化剂活性有关.反应动力学测试显示催化剂低温可还原氧物种有利于HCl在催化剂表面的吸附和活化,而催化剂表面的氧空位可以促进氧分子的吸附和活化.     

丙烷选择氧化的铋钼复合氧化物催化剂结构和催化性能

 应用X射线衍射（XRD）,傅里叶变换激光拉曼光谱（FT－LRS）和微型催化反应装置等测试手段研究了丙烷选择氧化的Bi－Mo复合氧化物催化剂的结构和催化性能．结果表明,Bi组分是丙烷催化氧化脱氢为丙烯的主要活性组分,而丙烯醛选择性的大小与Bi－Mo复合氧化物催化剂的组成和结构密切相关．不同组成的Bi－Mo复合氧化物催化剂在丙烷转化率（～28．0％）相近的情况下,其丙烯醛选择性随Mo／（Mo＋Bi）原子比的增加先逐渐增加,在Mo／（Mo＋Bi）原子比为0．50时达极大值（～28．1％）．随Mo／（Mo＋Bi）原子比进一步增加,丙烯醛选择性又急剧下降．XRD和FT－LRS结果表明,Bi2O3和MoO3之间可形成二元Bi－Mo－O晶相固溶体,从而显著提高了催化剂对选择氧化反应的催化性能．尤其是当α－Bi2（MoO4）3和γ－Bi2MoO6两相共存时,Bi－Mo复合氧化物催化剂具有较优良的选择氧化催化性能．γ－Bi2MoO6参与了α－Bi2（MoO4）3对丙烷的选择氧化,加速了选择氧化活性氧物种的再生．     

Cr2O3-Co3O4／SiO2对十八醇氧化生成十八酸反应的催化性能

 制备了一系列不同Cr／Co比例的Cr2O3－Co3O4／SiO2催化剂，并用XRD，FT－IR和BET等手段对催化剂进行了表征；考察了催化剂对十八醇氧化生成十八酸反应的催化性能，及反应条件（反应温度和反应时间）对催化性能的影响，确定了最佳反应条件．结果表明，金属硝酸盐在773K焙烧后转变成相应的氧化物并负载于二氧化硅上．Cr2O3－Co3O4／SiO2催化剂对十八醇氧化反应有很高的催化活性，十八酸选择性最高可达99．93％，收率可达52．44％．Cr2O3－Co3O4／SiO2催化剂的活性明显高于单一的Cr2O3／SiO2或Co3O4／SiO2催化剂     

LaCo0.9Cu0.1O3的蔗糖溶胶-凝胶法合成及二甲苯催化氧化性能研究

蔗糖溶胶 凝胶法合成了稀土钙钛矿型复合氧化物LaCo0 .9Cu0 .1 O3,并对其进行了XRD ,BET ,TPR表征和二甲苯催化氧化性能测试 ,并与柠檬酸溶胶 凝胶法作了比较。结果表明 ,蔗糖作为络合剂成胶和干胶容易 ,粒径较小 ,具有进一步降低LaCo0 .9Cu0 .1 O3形成温度的作用 ,以蔗糖作为络合剂在 70 0℃所制备的催化剂LaCo0 .9Cu0 .1 O3低温活性较好。     

CeO2-ZrO2复合氧化物对金属蜂窝整体催化剂性能的影响

 用浸渍法制备了不同比例的CeO2－ZrO2复合氧化物，并用XRD，H2－TPR和BET等研究了复合氧化物的晶相、还原性能及热稳定性．结果表明，所制备的CeO2－ZrO2复合氧化物形成了固溶体，Ce0．6Zr0．4O2比Ce0．90Zr0．10O2更容易被H2还原；1100℃老化后，晶胞参数无明显变化，比表面积仍有11．8m2／g．模拟二冲程摩托车尾气组成，对用贵金属Pt，Pd，Rh与CeO2及CeO2－ZrO2固溶体所制备的催化剂进行了活性评价．结果显示，1100℃老化后，催化剂仍具有很高的氧化活性．在贫氧区，Pt－Pd－Rh／Ce0．6Zr0．4O2－Al2O3对碳氢化合物氧化的催化活性则有一定的优势，是一种具有较高热稳定性的催化剂．     

CuCrO2和CrCr2O4间相互作用对体系结构和催化性能的影响

 以柠檬酸络合法制备了CuCrO2和CuCr2O4两相共生的Cu－Cr－O催化剂体系．由于两相共生而相互作用，两相组成的样品中，样品颗粒较小，比表面积增大，催化CO－O2反应的活性提高．当样品中n（Cu）／n（Cr）＝0．7时，两相含量最为接近，显示出最高的催化活性．CO－O2反应过程中，气相中的CO与样品表面的氧原子作用．在两相共生而相互作用的过程中，CuCrO2和CuCr2O4的体相结构没有变化．各样品催化活性的不同是由其表面性质的差异引起的．TPR和XPS分析结果表明：两相共生而相互作用，修饰了样品的表面性质，使样品表面含有更多的活性氧，提高了样品的催化活性．     

纳米Cr2O3系列催化剂上CO2氧化乙烷脱氢制乙烯反应

 采用溶胶－凝胶法和共沸蒸馏法耦合技术制备了纳米Cr2O3催化剂，并采用共沉淀法和共沸蒸馏法耦合技术制备了纳米Cr2O3／Al2O3，Cr2O3／ZrO2和Cr2O3／MgO复合催化剂．应用BET，XRD，XPS，TPR和TEM等物理化学方法对催化剂的结构和物化性质进行了表征，并考察了该系列催化剂上CO2氧化乙烷脱氢制乙烯的反应性能．结果表明，纳米Cr2O3催化剂上乙烷和CO2的转化率均明显高于常规Cr2O3催化剂，但乙烯的选择性低于常规Cr2O3催化剂；纳米复合催化剂中的复合成分显著影响催化剂的催化性能．其中，10％Cr2O3／MgO纳米复合催化剂在温度为973K时，乙烷转化率和乙烯选择性分别可达到61．54％和94．79％．纳米催化剂表面Cr的还原性以及Cr6＋／Cr3＋比值是影响乙烷转化率和乙烯选择性的重要因素．     

复合氧化物CeO2-Co3O4催化氧化CO的性能

以共沉淀法制备CeO2-Co3O4复合氧化物，研究复合氧化物CeO2-Co3O4低温催化氧化CO的性能。通过采用热重分析（TG）、比表面积测试（BET）、X射线衍射分析（XRD）、程序升温还原（TPR）以及原位红外漫反射（FT-IR）等表征手段，详细探讨了铈含量对于复合氧化物CeO2-Co3O4低温催化氧化CO性能的影响。结果表明：复合氧化物CeO2-Co3O4催化氧化CO的性能明显优于单一氧化物CeO2和CO3O4，     

Ce1-xFexO2复合氧化物催化剂的制备及其对甲烷的催化燃烧性能

采用柠檬酸溶胶-凝胶法和微波技术制备了Ce1-x Fex O2复合氧化物，以甲烷催化燃烧为探针反应测定了催化剂的活性及XRD、DRS、BET和TPR进行了表征。结果表明，Ce1-x Fex O2复合氧化物为介孔材料，所制得的复合氧化物在x≤0．2时以单一立方萤石结构的Ce1-x Fex O2固溶体存在，x〉0．2时形成了立方萤石结构Ce1-x Fex O2固溶体和少量的CeFeO3混合相。Ce1-x Fex O2固溶体的甲烷催化燃烧活性高于单组分CeO2，且随着x的不同而变化，其中以Ce0.9 Fe0.1 O2固溶体的催化活性最高。     

柱撑化合物Zn2Al-PW11Z的结构模型及酯化活性

杂多化合物是性能优异的酸型和氧化型或双功能催化剂[1－4]，而通式为的阴离子粘土通常具有减催化或还原催化性能[5，6]．因此，从在分子及原子水平上设计催化剂，调控催化性能观点出发，人们期望将体积较大的杂多阴离子嵌入阴离子粘土层间，合成大层间距的新型柱撑微孔材料．1988年Pinnavaia等人[7]首次报导了Zn2Al－V10O28是具有2．0nm孔径分布的中微孔材料．最近，笔者将单取代型Keggin结构杂多阴离子GeW11O39Z（H2O）6－（其中Z＝Ni2 和Cu2 ）和缺位Keggin结构的GeW11O嵌入Zn2Al－NO3层间，合成了通道高度为0．9nm的新型柱撑…     

CeO2-TiO2复合氧化物的制备、表征及其对CO氧化的催化性能

采用溶胶-凝胶法制备了一系列不同n(Ce)/n(Ti)的CeO2-TiO2复合氧化物,对复合氧化物的物相结构、形貌特征、比表面积和氧化还原性质进行了表征,并考察了复合氧化物对CO氧化反应的催化性能.结果表明,n(Ce)/n(Ti)>0.10时,复合氧化物为无定形结构;n(Ce)/n(Ti)=0.10~0.30时,复合氧化物失去CeO2和TiO2各自的特征,形成CeO2-TiO2固溶体,具有较大的比表面积.CeO2-TiO2复合氧化物本身对CO氧化反应的催化活性不如TiO2或CeO2的高,但Pd/CeO2-TiO2比Pd/TiO2或Pd/CeO2具有更高的催化活性.     

Oxidation of Carbon Monoxide on Co-, Ni-, and Cu-containing Catalysts Prepared by Pyrolysis of Metal β-Diketonates on Synthetic Foamed Ceramics

Catalytic systems containing Co, Ni, and Cu composite coatings prepared by gas-phase thermolysis of metal acetylacetonates and hexafluoroacetylacetonates on synthetic foamed ceramics were suggested for oxidation of CO to CO₂. The relative activities of the catalysts and the kinetic and activation parameters of CO oxidation were determined. The catalytic activity depends on the catalyst preparation procedure.     

Effect of preparation procedure on the properties of CeO2

The effect of preparation procedure on the physicochemical and catalytic properties of CeO₂ was studied. Differences in the electronic and structural characteristics of CeO₂ depending on preparation procedure and treatment temperature were found using X-ray diffraction analysis, transmission electron microscopy, UV-visible electronic spectroscopy, and X-ray photoelectron spectroscopy. With the use of the temperature-programmed reaction with CO, it was demonstrated that CeO₂ samples with a high concentration of point defects—oxygen vacancies caused by the presence of Ce³⁺—were characterized by an increased mobility of bulk oxygen. The samples of CeO₂ with a high concentration of structural defects—micropores of size 1–2 nm and stepwise vicinal faces in crystallites—exhibited a high catalytic activity in the reaction of CO oxidation.     

纳米级ZnO/MgO固体的合成及其对CO的氧化活性

The ZnO/MgO solid samples containing the ZnO nanoparticles of controllable size were prepared using colloidal technique. The catalytic performance of the ZnO/MgO samples for the CO oxidation was measured. It was revealed that the rate of the CO oxidation reaction on the ZnO nanoparticles with variable average radius (2.01-2.29 nm) shows nonmonotonic dependence caused by the quantum-confinement effect.     

Cu/SiO2纳米气凝胶的组成及催化氧化CO性能研究

以硝酸铜、 正硅酸乙酯和硝酸铈为原料, 利用溶胶-凝胶-超临界流体干燥技术制备了不同n(Cu)/n(Si)的用于CO催化氧化的Cu/SiO2系列气凝胶催化剂. 利用TEM、 XRD、 物理吸附、 微型反应器和气相色谱等对试样进行了表征. TEM观察结果显示, 试样中含有介孔的气凝胶结构, 5 nm左右的Cu粒子均匀地分布在SiO2的网络组织中. BET分析结果表明, 试样的比表面积均在140 m2/g以上. XRD分析结果显示, 添加铈前后, 试样的物相发生了从Cu 2+ →Cu+ →Cu的转变, 使试样的催化活性进一步提高. 试样的催化氧化CO活性表明, 组分中铜含量的不同及铜的不同物种直接影响试样的催化氧化CO的活性, 当组分中n(Cu)/n(Si)=2时, Cu/SiO2试样上CO完全氧化的温度降为210 ℃; 于400 ℃低温焙烧, 可使试样中有效活性组分全部转变成纳米晶CuO, 并进一步降低了CO完全转变成CO2的温度; 添加少量铈组分, 使试样催化氧化CO的tstart, t50及t90温度提前20 ℃以上, Cu/SiO2试样催化氧化CO动力学研究结果显示, 试样降低CO氧化温度的实质是降低了CO氧化的反应活化能.     

Relationship between structure and CO oxidation activity of ceria-supported gold catalysts

Gold catalysts supported on cerium oxide were prepared by solvated metal atom dispersion (SMAD), by deposition-precipitation (DP), and by coprecipitation (CP) methods and were characterized by X-ray diffraction (XRD), temperature programmed reduction (TPR), and X-ray photoelectron spectroscopy (XPS). The catalytic activity was tested in the CO oxidation reaction. The structural and surface analyses evidenced the presence of a modified ceria phase in the case of the DP sample and the presence of pure ceria and gold metal crystallites in the case of the SMAD and CP samples. The DP sample, after a mild treatment in air at 393 K, exhibited only ionic gold, and it was very active below 273 K. By comparing the activities of the different catalysts, it is suggested that the presence of small gold particles, as obtained by the SMAD technique, is not the main requisite for the achievement of the highest CO conversion. The strong interaction between ionic gold and ceria, by enhancing the ceria surface oxygen reducibility, may determine the particularly high activity.     

Co3O4/CeO2 CO氧化的原位红外光谱研究

采用沉淀氧化法制备了Co₃O₄/CeO₂催化剂。分别在干、湿条件下进行了一氧化碳氧化反应研究。运用FT-IR表征手段,在钴铈复合氧化物上进行了CO吸附及CO/O₂共吸附研究。结果表明,与纯的Co₃O₄样品相比,Co₃O₄/CeO₂具有明显的抗湿气能力。Co₃O₄/CeO₂催化剂在进行CO氧化时,表面形成了类碳酸盐物种。当环境温度低于453 K时,催化剂上类碳酸盐的生成与形成类碳酸盐物种后受热分解存在着动态平衡。当环境温度高于493 K,催化剂上生成的类碳酸盐物全部受热分解。氧化铈的加入提高了催化剂的抗湿气性能。较小粒径的Co₃O₄与CeO₂产生的强相互作用可使CeO₂向Co₃O₄提供氧,因而间接提供了CO氧化需要的氧。     

金属有机骨架材料MIL-53(Al)负载纳米Pd颗粒：一种CO氧化的活性催化剂

通过等体积浸渍法制备了金属有机骨架材料MIL-53(Al) (MIL：Materials of Institut Lavoisier)负载纳米Pd催化剂. 采用X射线衍射(XRD)、透射电子显微镜(TEM)和X射线光电子能谱(XPS)等手段对催化剂的结构进行了表征. 催化剂在反应前后XRD衍射峰保持不变,说明载体MIL-53(Al)具有良好的稳定性. 采用TEM对催化剂进行表征,结果表明,MIL-53(Al)的多孔晶体结构有助于形成高度分散的纳米Pd颗粒,样品2.7% (w) Pd/MIL-53 中Pd颗粒的平均粒径为2.21 nm. 该催化剂在CO氧化反应中表现出较高的催化活性,115 ℃达到完全转化. 同时催化剂可循环使用,多次反应后催化活性和催化剂结构都保持稳定.     

Effects of reduction temperature and metal-support interactions on the catalytic activity of Pt/gamma-Al2O3 and Pt/TiO2 for the oxidation of CO in the presence and absence of H2

TiO2- and gamma-Al2O3-supported Pt catalysts were characterized by HRTEM, XPS, EXAFS, and in situ FTIR spectroscopy after activation at various conditions, and their catalytic properties were examined for the oxidation of CO in the absence and presence of H2 (PROX). When gamma-Al2O3 was used as the support, the catalytic, electronic, and structural properties of the Pt particles formed were not affected substantially by the pretreatment conditions. In contrast, the surface properties and catalytic activity of Pt/TiO2 were strongly influenced by the pretreatment conditions. In this case, an increase in the reduction temperature led to higher electron density on Pt, altering its chemisorptive properties, weakening the Pt-CO bonds, and increasing its activity for the oxidation of CO. The in situ FTIR data suggest that both the terminal and bridging CO species adsorbed on fully reduced Pt are active for this reaction. The high activity of Pt/TiO2 for the oxidation of CO can also be attributed to the ability of TiO2 to provide or stabilize highly reactive oxygen species at the metal-support interface. However, such species appear to be more reactive toward H2 than CO. Consequently, Pt/TiO2 shows substantially lower selectivities toward CO oxidation under PROX conditions than Pt/gamma-Al2O3.     

Promotion effect of Au single-atom support graphene for CO oxidation

CO oxidation is a vital catalytic reaction for environmental purification, facing challenges due to the catalysts applied to oxidize CO are mainly rare and expensive noble catalysts. Since the high atomic availability, catalytic efficiency, and selectivity of single-atom catalysis, it has been widely studied and proven to be brilliant in CO oxidation. Au single-atom catalysts are regarded as excellent single-atom catalysts in oxidizing CO, whose progress is limited by the indistinct understanding of the reaction mechanism and role of the active atom. Hence, DFT calculation was used to investigate CO oxidation processes, active mechanisms, and the role of Au single-atom. Graphene involving prominent physical and chemical properties was selected as a model supporter. The single-atom support graphene materials exhibit better CO oxidation activities than pristine graphene, among which CO oxidation property on Au/GP is the highest with a 0.38 eV rate-determining barrier following ER mechanism. The outstanding performances including excellent electronic structures, adsorption properties, and strong activation of intermediate products contribute to the high CO oxidation activity of Au/GP, and the Au single-atom is the active center. Our work provides a novel guide for single-atom catalytic CO oxidation, accelerating the development of single-atom catalysis.