制备方法对氧化锰八面体分子筛的NH_3选择性催化还原NO_x性能的影响

采用不同方法制备了一系列氧化锰八面体分子筛(OMS-2)催化剂,考察了制备方法对其低温NH3-SCR催化性能的影响,并采用BET、XRD、Raman、H2-TPR、XPS和TEM等手段对催化剂的物化性质进行表征。结果表明,OMS-2催化剂在50~150℃时其低温SCR活性明显优于MnOx催化剂,OMS-2催化剂在120℃时NOx转化率接近100%。此外,不同的制备方法对OMS-2催化剂的SCR脱硝活性影响明显。其中,固相法制备的OMS-2催化剂的SCR活性最佳。H2-TPR测试结果表明,OMS-2更容易发生氧化还原反应,MnOx还原峰对应的温度较高。XRD、TEM和XPS分析结果表明,低结晶度和高分散性的无定形催化剂有利于低温SCR反应,较高的表面晶格氧和无定形MnO2物种是OMS-2催化剂具有优异低温SCR活性的主要原因。     

活性炭表面担载氧化锰复合电极的电化学电容性能

通过在两种商品活性炭XC-72(比表面250m2·g-1)和YEC-8(比表面1726m·2g-1)电极表面涂刷Mn(NO3)2,并在200℃进行热分解得到表面担载氧化锰的复合材料电极.采用扫描电子显微镜(SEM)和X射线衍射(XRD)表征电极的形貌和氧化锰的晶体结构,采用循环伏安、恒流充放电和交流阻抗考察了不同电极的电化学电容性能.结果表明,Mn(NO3)2在200℃的热解产物是α-Mn2O3和α-Mn3O4的混合物.当C和MnOx的质量比为2∶1和9∶1时,XC-72/MnOx中氧化锰的比电容分别达到499和435F·g-1,YEC-8/MnOx中氧化锰的比电容分别达到554和606F·g-1,表明氧化锰的赝电容对电极比电容的贡献十分显著.     

TiO_2晶相对MnO_x/TiO_2催化剂催化NO氧化性能的影响（英文）

以浸渍在不同晶相TiO2(金红石型(R)、锐钛矿型(A)和P25型(P))上的锰基催化剂为对象,研究了TiO2晶相对MnOx/TiO2催化剂催化NO氧化活性的影响.结果表明,MnOx/TiO2(P)催化剂活性最高,NO转化率在300°C及GHSV=20000 h–1条件下可达83%.各催化剂活性顺序为MnOx/TiO2(P)MnOx/TiO2(A)MnOx/TiO2(R).采用X射线粉末衍射、场发射扫描电子显微镜、X射线光电子能谱、H2程序升温还原和O2程序升温脱附等手段研究了TiO2晶相影响MnOx/TiO2催化剂催化活性的作用机理.结果表明,相比于A和R型TiO2,P型TiO2能够增加MnOx在其表面的分散度并抑制催化剂颗粒的团聚和粘连,且更有利于Mn2O3的生成,而后者催化NO氧化活性比其它MnOx更高;此外,P型TiO2可以增加MnOx尤其是Mn2O3的还原性,并可促进O2–从M3+–O键的脱附.     

Pd/MnOx+Pd/γ-Al2O3整体式催化剂降解地表臭氧

用高锰酸钾与硝酸锰氧化还原反应制备了高活性的氧化锰(MnO x)催化组分,用胶溶法制备了高比表面积的γ-Al2O3载体,分别用等体积浸渍法制备了Pd/MnO x和Pd/γ-Al2O3催化剂,然后将两者机械混合涂覆于堇青石上制得Pd/MnO x+Pd/γ-Al2O3整体式催化剂。采用X射线衍射(XRD)、X射线光电子能谱(XPS)、程序升温还原(H2-TPR)和低温N2吸附-脱附对催化剂进行了表征。考察了在300至700℃焙烧MnO x对催化剂降解地表O3活性的影响。结果表明,Pd和MnO x之间存在协同作用;MnO x焙烧温度对催化剂活性有一定的影响,其中以600℃焙烧时催化剂的活性最高,O3的起始(12℃)转化率达到88%,完全转化温度为18℃。MnOx的物相和催化剂表面的吸附氧物种对催化活性影响较大,适当比例的MnO2和Mn2O3共存有利于O3分解,表面吸附氧为O3分解的活性氧物种。     

制备方法对Pd-MnOx/γ-Al2O3催化剂分解地表O3性能的影响（英文）

分别用溶胶凝胶法和分步沉淀法制备了MnOx+γ-Al2O3和MnOx/γ-Al2O3,用等体积浸渍法将等量的Pd(NO3)2分别浸渍于其上,再将它们分别涂覆于堇青石上,得到不同物理化学性质的整体式催化剂,并采用X射线衍射、X射线光电子能谱、程序升温还原和低温N2吸附-脱附等技术对催化剂进行表征.结果表明,制备方法和MnOx焙烧温度明显影响催化剂中MnOx的物相、表面Mn物种和表面活性氧物种的分布及织构性质.活性测试结果表明,两种制备方法得到的催化剂于16–90 oC,380000–580000 h–1条件下均可将0.6μL·L–1 O3完全分解;尤其是溶胶凝胶法制备的Pd/γ-Al2O3+MnOx/γ-Al2O3催化剂分解O3活性较好,催化剂表面Mn2+:Mn3+:Mn4+=1.7:1:3(mol).     

制备方法对Pd-MnOx/γ-Al2O3催化剂分解地表O3性能的影响（英文）

分别用溶胶凝胶法和分步沉淀法制备了MnOx+γ-Al2O3和MnOx/γ-Al2O3,用等体积浸渍法将等量的Pd(NO3)2分别浸渍于其上,再将它们分别涂覆于堇青石上,得到不同物理化学性质的整体式催化剂,并采用X射线衍射、X射线光电子能谱、程序升温还原和低温N2吸附-脱附等技术对催化剂进行表征.结果表明,制备方法和MnOx焙烧温度明显影响催化剂中MnOx的物相、表面Mn物种和表面活性氧物种的分布及织构性质.活性测试结果表明,两种制备方法得到的催化剂于16–90 oC,380000–580000 h–1条件下均可将0.6μL·L–1 O3完全分解;尤其是溶胶凝胶法制备的Pd/γ-Al2O3+MnOx/γ-Al2O3催化剂分解O3活性较好,催化剂表面Mn2+:Mn3+:Mn4+=1.7:1:3(mol).     

制备方法对Pd-MnO_x/γ-Al_2O_3催化剂分解地表O_3性能的影响(英文)

分别用溶胶凝胶法和分步沉淀法制备了MnOx+γ-Al2O3和MnOx/γ-Al2O3,用等体积浸渍法将等量的Pd(NO3)2分别浸渍于其上,再将它们分别涂覆于堇青石上,得到不同物理化学性质的整体式催化剂,并采用X射线衍射、X射线光电子能谱、程序升温还原和低温N2吸附-脱附等技术对催化剂进行表征.结果表明,制备方法和MnOx焙烧温度明显影响催化剂中MnOx的物相、表面Mn物种和表面活性氧物种的分布及织构性质.活性测试结果表明,两种制备方法得到的催化剂于16–90 oC,380000–580000 h–1条件下均可将0.6μL·L–1 O3完全分解;尤其是溶胶凝胶法制备的Pd/γ-Al2O3+MnOx/γ-Al2O3催化剂分解O3活性较好,催化剂表面Mn2+:Mn3+:Mn4+=1.7:1:3(mol).     

新型铁锰复合氧化物催化低温脱除NOx

采用溶胶-凝胶法合成了一系列铁锰复合氧化物催化剂, 利用X射线衍射(XRD)对催化剂的活性相态进行研究, 并考察了铁锰摩尔比及焙烧温度对催化性能的影响. 结果表明, 该催化剂体系在低温(80-220 ℃)下选择性催化氨还原NOx反应中显示出优异的活性. 其中Fe(0.4)-MnOx(500)(即摩尔比n(Fe)/(n(Fe)+n(Mn))=0.4, 焙烧温度500 ℃)催化剂具有最佳低温催化活性, 在空速30000 h-1, 温度80 ℃的条件下, NOx转化效率达到90.6%, N2选择性达100%. Fe-MnOx复合氧化物催化剂中形成的Fe3Mn3O8晶相有利于促进NO氧化成NO2, 从而提高低温选择性催化还原的活性.     

整体式锰基催化剂催化分解地表臭氧

通过焙烧碳酸锰粉末制备了高活性含缺陷氧原子的氧化锰材料(MnOx, x=1.6～2.0), 用胶溶法制备了高比表面积的SiO2-Al2O3载体,然后用等体积浸渍法制备了不同MnOx担载量的Pd-MnOx/SiO2-Al2O3系列催化剂. 结果表明,催化剂活性随MnOx含量的增加而增加,但无载体的MnOx催化剂易脱落,活性降低. 在空速(GHSV)为 360 000 h-1 的条件下, MnOx含量为80%的催化剂对O3的完全转化温度(T100)为30 ℃; 在GHSV=660 000 h-1 时, MnOx含量在80%～90%的催化剂活性最高, T100 为45～50 ℃, 能满足在汽车运行时空气与汽车水箱瞬时接触温度的要求. 在45 ℃和 510 000 h-1 条件下对MnOx担载量为80%的催化剂进行 95 h 寿命测试后, O3的转化率大于90%, 说明催化剂具有很强的抗失活能力.     

新型铁锰复合氧化物催化低温脱除NOx

采用溶胶-凝胶法合成了一系列铁锰复合氧化物催化剂,利用X射线衍射(XRD)对催化剂的活性相态进行研究,并考察了铁锰摩尔比及焙烧温度对催化性能的影响.结果表明,该催化剂体系征低温(80-220℃)下选择性催化氨还原NOx反应中显示出优异的活性.其中Fe(0.4)-MnOx(500)(即摩尔比n(Fe)/(n(Fe)+n(Mn))=0.4,焙烧温度500℃)催化剂具有最佳低温催化活性,在空速30000 h-1,温度80℃的条件下,NOx转化效率达到90.6%,N2 选择性达100%.Fe-MnOx复合氧化物催化剂中形成的Fe3Mn3O8晶相有利于促进NO氧化成NO2,从而提高低温选择性催化还原的活性.     

Catalytic Performance of MnOx Nanorods in Aerobic Oxidation of Benzyl Alcohol

Various manganese oxide nanorods with similar one-dimensional morphology were prepared by calcination of MnOOH nanorods under different gas atmosphere and at different temper-atures, which were synthesized by a hydrothermal route. The morphology and structure of MnO_x catalysts were characterized by a series of techniques including X-ray photoelectron spectroscopy, scanning electron microscopy, transmission electron microscopy, and tempera-ture programmed reduction (TPR). The catalytic activities of the prepared MnO_x nanorods were tested in the liquid phase aerobic oxidation of benzyl alcohol, which follow a sequence as MnO₂>Mn₂O₃≈Mn₃O₄>MnOOH with benzaldehyde being the main product. On the basis of H₂-TPR results, the superior activity of MnO₂ is ascribed to its lower reduction temperature and therefore high oxygen mobility and excellent redox ability. Moreover, a good recycling ability was observed over MnO₂ catalysts by simply thermal treatment in air.     

Effect of Calcination Temperature on the Structure and Catalytic Properties of MnO<Subscript><Emphasis Type="Italic">x</Emphasis></Subscript>/Ca<Subscript>2</Subscript>O<Subscript>3</Subscript> in the Reaction of CO and Ethane Oxidation

Effect of the calcination temperature of the MnOx/Ga2O3 system on its structural and catalytic properties in the reaction of oxidation of CO and hydrocarbons. The dependences of the catalytic activity of MnO _x /Ga₂O₃ in the reactions of CO and ethane oxidation on the calcination temperature exhibit an extremal behavior. The maximum values of activity are observed upon calcination of the system at 700°C, i.e., at the temperature that is limiting for the existence of a solid solution of manganese ions in γ-Ga₂O₃. The structural changes occurring with increasing calcination temperature are accompanied by a substantial decrease in the specific surface area of a sample. The observed rise in the specific catalytic activity (by a factor of ~7 upon an increase in the preliminary-calcination temperature from 600 to 800°C) confirms that the thermal activation effect exists for the given system.     

Total Oxidation of Methane Over La, Ce and Y Modified Manganese Oxide Catalysts

A series of catalysts based on high specific surface area MnO₂ precursor, and modified by La, Ce or Y ions were prepared and applied for methane deep oxidation. XRD and BET results indicate that La, Ce and Y ions as additives can impede the crystallization of catalysts at high temperatures. Thus, some catalysts that can maintain much higher specific surface area than unmodified MnOx were obtained. The main species of all catalysts are proved to be crystalline or amorphous Mn₂O₃ by XRD and H₂-TPR. The activities for methane total oxidation over these catalysts are compared with each other. It is found that all modified catalysts show higher activities than unmodified MnOx below 420°C, but show a little lower activity above this temperature.     

Effect of the oxidation state of manganese in the manganese oxides used in the synthesis of Mn-substituted cordierite on the properties of the product

Catalysts based on Mn-substituted cordierite 2MnO · 2Al₂O₃ · 5SiO₂ have been synthesized using different manganese oxides (MnO, Mn₂O₃, and MnO₂) at a calcination temperature of 1100°C. The catalysts differ in their physicochemical properties, namely, phase composition (cordierite content and crystallinity), manganese oxide distribution and dispersion, texture, and activity in high-temperature ammonia oxidation. The synthesis involving MnO yields Mn-substituted cordierite with a defective structure, because greater part of the manganese cations is not incorporated in this structure and is encapsulated and the surface contains a small amount of manganese oxides. This catalyst shows the lowest ammonia oxidation activity. The catalysts prepared using Mn₂O₃ or MnO₂ are well-crystallized Mn-substituted cordierite whose surface contains different amounts of manganese oxides differing in their particle size. They ensure a high nitrogen oxides yield in a wide temperature range. The product yield increases with an increasing surface concentration of Mn³⁺ cations. The highest NO_x yield (about 76% at 800–850°C) is observed for the MnO₂-based catalyst, whose surface contains the largest amount of manganese oxides.     

Effect of the Calcination Temperature and Composition of the MnO<Subscript><Emphasis Type="Italic">x</Emphasis></Subscript>–ZrO<Subscript>2</Subscript> System on Its Structure and Catalytic Properties in a Reaction of Carbon Monoxide Oxidation

The effect of the calcination temperature and composition of the MnO_x–ZrO₂ system on its structural characteristics and catalytic properties in the reaction of CO oxidation was studied. According to X-ray diffraction analysis and H₂ thermo-programmed reduction data, an increase in the calcination temperature of Mn_0.12Zr_0.88O₂ from 450 to 900°C caused a structural transformation of the system accompanied by the disintegration of solid solution with the release of manganese ions from the structure of ZrO₂ and the formation of, initially, highly dispersed MnO_x particles and then a crystallized phase of Mn₃O₄. The dependence of the catalytic activity of MnO_x–ZrO₂ in the reaction of CO oxidation on the calcination temperature takes an extreme form. A maximum activity was observed after heat treatment at 650–700°C, i.e., at limiting temperatures for the occurrence of a solid solution of manganese ions in the cubic modification of ZrO₂. If the manganese content was higher than that in the sample of Mn_0.4Zr_0.6O₂, the phase composition of the system changed: the solid solution phase was supplemented with Mn₂O₃ and β-Mn₃O₄ phases. The samples of Mn_0.4Zr_0.6O₂–Mn_0.6Zr_0.4O₂ exhibited a maximum catalytic activity; this was likely due to the presence of the highly dispersed MnO_x particles, which were not the solid solution constituents, on their surface in addition to an increase in the dispersity of the solid solution.     

Precursor-Support Interactions in Silica-Supported Manganese Oxide Catalysts

Summary. Catalyst materials investigated in this study were obtained by calcination of impregnated silica with Mn(CH₃COO)₂·4H₂O and MnC₂O₄·2H₂O, so as to yield 10wt% Mn/SiO₂. The precursor compounds as well as pure and impregnated silica support were calcined at 600 and 1000°C in a static air atmosphere for 5h. Structural characteristics of the catalysts thus obtained were investigated by DTA, TG, XRD, IR and DRS. N₂ adsorption at –195°C was used for the assessment of surface texture of the test materials. Results of structural characterisation of catalysts obtained by calcination of manganese acetate-impregnated silica at 1000°C indicated the presence of strong silica-precursor interactions. Species of manganese silicates were detectable. Moreover, the decomposition of manganese acetate enhanced the transformation of amorphous silica into well crystallised -quartz. In contrast, Mn₂O₃, Mn₃O₄, and minor proportions of MnO were detected in the catalysts derived from the manganese oxalate-impregnated silica. This has been ascribed to much weaker precursor/support interactions in the oxalate-impregnated silica than the acetate-impregnated one.     

The formation and physicochemical characterization of Al2O3-doped manganese ferrites

Mn/Fe mixed oxide solids doped with Al₂O₃ (0.32-1.27 wt.%) were prepared by impregnation of manganese nitrate with finely powdered ferric oxide, then treated with different amounts of aluminum nitrate. The obtained samples were calcined in air at 700-1000 °C for 6 h. The specific surface area (S_BET) and the catalytic activity of pure and doped precalcined at 700-1000 °C have been measured by using N₂ adsorption isotherms and CO oxidation by O₂. The structure and the phase changes were characterized by DTA and XRD techniques. The obtained results revealed that Mn₂O₃ interacted readily with Fe₂O₃ to produce well-crystallized manganese ferrite (MnFe₂O₄) at temperatures of 800 °C and above. The degree of propagation of this reaction increased by Al₂O₃-doping and also by increasing the heating temperature. The treatment with 1.27 wt.% Al₂O₃ followed by heating at 1000 °C resulted in complete conversion of Mn/Fe oxides into the corresponding ferrite phase. The catalytic activity and S_BET of pure and doped solids were found to decrease, by increasing both the calcination temperature and the amount of Al₂O₃ added, due to the enhanced formation of MnFe₂O₄ phase which is less reactive than the free oxides (Mn₂O₃ and Fe₂O₃). The activation energy of formation (ΔE) of MnFe₂O₄ was determined for pure and doped solids. The promotion effect of aluminum in formation of MnFe₂O₄ was attributed to an effective increase in the mobility of reacting cations.     

NMR and FT-IR Investigation of Spinel LiMn2O4 Cathode Prepared by the Tartaric Acid Gel Process

The structure of the lithium manganese tartrate precursor and the synthesis mechanism of LiMn₂O₄ were investigated by FT-IR, NMR, TG/DSC, and XRD in this study. The results of FT-IR and ⁷Li and ¹³C NMR measurements revealed that lithium ions bond with carboxylic acid ligands and the O–H stretching modes of tartaric acid. Manganese ion bonds only with carboxylic acid. Lithium and manganese ions were trapped homogeneously on an atomic scale throughout the precursor. Such a structure eliminates the need for long-range diffusion during the formation of lithium manganese oxides. Therefore, spinel LiMn₂O₄ was synthesized at temperatures as low as 300°C. In this work, the electrochemical properties of Li/Li_xMn₂O₄ were studied. It is clear that the discharge curves exhibit two pseudo plateaus as the LiMn₂O₄ is fired to higher temperatures. The discharge capacity of LiMn₂O₄ increases from 84 to 117 mAh/g as the calcination temperature increases from 300 to 500°C. The LiMn₂O₄ powders calcined at low temperatures with a high specific surface area and an average valence of manganese exhibit a better cycle life.     

Preparation of Mn2O3 and Mn3O4 nanofibers via an electrospinning technique

Thin PVA/manganese acetate composite fibers were prepared by using sol-gel processing and electrospinning technique. After calcinations of the above precursor fibers, Mn₂O₃ and Mn₃O₄ nanofibers with a diameter of 50-200 nm could be successfully obtained. The fibers were characterized by TG-DTA, Scanning electron microscopy, FT-IR, WAXD, respectively. The results showed that the crystalline phase and morphology of nanofibers were largely influenced by the calcination temperature.     

Nanorods of manganese oxides: Synthesis, characterization and catalytic application

Single-crystalline nanorods of β-MnO₂, α-Mn₂O₃ and Mn₃O₄ were successfully synthesized via the heat-treatment of γ-MnOOH nanorods, which were prepared through a hydrothermal method in advance. The calcination process of γ-MnOOH nanorods was studied with the help of Thermogravimetric analysis and X-ray powder diffraction. When the calcinations were conducted in air from 250 to 1050 °C, the precursor γ-MnOOH was first changed to β-MnO₂, then to α-Mn₂O₃ and finally to Mn₃O₄. When calcined in N₂ atmosphere, γ-MnOOH was directly converted into Mn₃O₄ at as low as 500 °C. Transmission electron microscopy (TEM) and high-resolution TEM were also used to characterize the products. The obtained manganese oxides maintain the one-dimensional morphology similar to the precursor γ-MnOOH nanorods. Further experiments show that the as-prepared manganese oxide nanorods have catalytic effect on the oxidation and decomposition of the methylene blue (MB) dye with H₂O₂.