氧化钛负载脱硝催化剂的碱中毒过程：氧化钒的保留和氧化钨的牺牲

V2O5-WO3/TiO2催化剂目前已广泛用于电厂和工业锅炉燃烧废气脱硝,但燃烧原料煤及石油中含有的杂质元素碱金属与碱土金属元素可吸附在催化剂上,不仅会减少催化剂酸性位的数量,还会与催化活性元素结合生成惰性物种,导致催化剂失活。因此,已有许多有关钒钨钛催化剂碱中毒的研究,从催化剂的氧化还原能力、酸性位损失及表面孔结构等方面进行了讨论。但这些研究大多集中在碱中毒对活性组分V2O5的影响及中毒催化剂的活性变化,很少涉及催化剂中WO3的作用,也缺乏有关不同活性元素与钾盐反应的实验证据。本文采用过量浸渍法制备了不同钒和钨含量的钒钨钛催化剂,研究了氯化钾对其氨法选择性催化还原(NH3-SCR)活性的失活效应。利用感应耦合等离子体、N2吸附、拉曼光谱、H2程序升温还原、NH3吸附红外光谱和NH3氧化活性等手段对新鲜和中毒催化剂的性质进行了表征,特别探讨了V2O5和WO3对催化剂抗碱中毒能力的贡献。
　　催化剂活性测试结果表明, V2O5含量越高,活性温度窗口越宽,而且含有WO3的三元催化剂活性高于V2O5/TiO2二元催化剂。催化剂的BET比表面积和孔结构取决于TiO2载体,随活性组分配比变化不大,说明催化剂物理结构性质并非影响活性的主要因素。原位红外光谱及H2程序升温还原测试结果表明,随V2O5含量提高,催化剂表面Br?nsted酸性位数量及氧化还原能力提高。作为反应的主要活性物种, V2O5在碱中毒处理后变成惰性的偏钒酸钾KVO3,使催化剂中Br?nsted酸性位减少,热稳定性下降,并削弱了催化剂的氧化还原能力,因此低钒含量的催化剂容易严重中毒失活。在高钒负载量(3%)时,部分V2O5在碱中毒后得以保留,从而使催化剂保持了一定的脱硝催化活性。
　　另外, WO3能给催化剂表面提供热稳定的酸性位,虽然WO3自身的氧化还原能力差,但其能改善V2O5的分散性,从而提高V2O5-WO3/TiO2催化剂的活性。除此之外, WO3在催化剂碱中毒过程中还能扮演牺牲剂,与钾反应生成钨酸钾(K2WO4),即在V2O5与钾离子结合形成KVO3的同时,部分WO3也会与钾反应形成K2WO4,可以使三元催化剂保留更多的活性V物种。因此,在所研究的催化剂中,高钒负载量的V2O5-WO3/TiO2催化剂表现出最好的抗碱中毒能力。
　　活性影响因素分析表明,对于新鲜催化剂,其表面吸附的NH3量足够多,催化剂活性与表面酸性相关度不大,脱硝效率主要取决于催化剂的氧化还原能力。但是,对于碱中毒处理后的催化剂,其表面吸附NH3的能力大大削弱,这时脱硝效率除了受催化剂氧化还原能力影响,在很大程度上也依赖于催化剂的表面酸性。     

Oxidic or metallic palladium: which is the active phase in pd-catalyzed aerobic alcohol oxidation?

In situ X-ray absorption spectroscopy combined with on-line catalytic measurements using FT-IR spectroscopy unequivocally identified that metallic palladium is the more active phase in the aerobic oxidation of benzyl alcohol than palladium oxide. The aerobic oxidation of benzyl alcohol in cyclohexane at 50 degrees C was low over oxidized 0.5%Pd/Al2O3 and 5%Pd/Al2O3 catalysts. XANES and EXAFS showed that the catalysts in the as-received state were almost fully oxidized and no reduction of the palladium constituent was observed during time-on-stream. After in situ reduction by hydrogen-saturated cyclohexane, the catalysts were much more active (over 50 times) than before reduction. Both XANES and EXAFS uncovered that the palladium constituent was mainly in a reduced state under these conditions of high catalytic activity. This demonstrates that metallic palladium is the active phase for alcohol dehydrogenation.     

丙烷选择氧化单斜 TeMo5O16 催化剂中钒掺杂的作用

 研究了在不同温度下 V 掺杂的单斜 TeMo5O16 催化剂上丙烷选择氧化反应性能. 结果发现, 在保持 TeMo5O16 相结构基本不变的条件下, V 的掺杂提高了催化剂的活性以及丙烯和丙烯醛等脱氢与选择氧化产物的收率. 通过程序升温表面反应、拉曼光谱、X 射线光电子能谱、X 射线衍射、程序升温还原和热重分析等手段对其原因进行了探讨. 结果表明, V 的掺杂引起催化剂表面金属–氧键发生变化, 提高了表面氧化还原中心的活性, 增加了酸性中心数目, 从而提高了催化剂活化丙烷能力. 同时, 较高的 V 掺杂量可以提高催化剂体相中晶格氧参与氧化还原的能力.     

Temperature-programmed desorption study of the selective oxidation of alcohols on silica-supported vanadium oxide

The partial oxidation of methanol and ethanol on silica-supported vanadium oxide catalysts was studied using temperature-programmed desorption (TPD), Raman spectroscopy, and diffuse reflectance infrared spectroscopy (DRIFTS). Methanol TPD results for V2O5/SiO2 samples as a function of vanadia loading in conjunction with X-ray diffraction data and Raman spectra indicated that dispersed vanadia on silica agglomerates into vanadia crystallites during a CH3OH TPD experiment. For ethanol-dosed samples, agglomeration of the dispersed vanadia was less severe, and it was possible to measure the activation energy for the dehydrogenation of adsorbed ethoxides to produce CH3CHO. Assuming a preexponential factor of 10(13) s(-1), the activation energy for this reaction was estimated to be 132 kJ/mol. The results of this study further demonstrate that there is a relatively weak interaction between vanadia and silica and suggest that adsorbed methoxide species help facilitate agglomeration of dispersed vanadia.     

Design, synthesis and characterization of vanadia-doped iron-oxide pillared montmorillonite clay for the selective catalytic oxidation of H2S

A series of vanadia-doped iron-oxide-pillared clays (V/Fe-PILCs) with various amounts of vanadia were prepared and their performance for the selective catalytic oxidation of H(2)S was investigated. V/Fe-PILCs were characterized using X-ray diffraction (XRD), surface area- and pore volume measurements, chemical analysis, Fourier-transform infrared (FTIR) spectroscopy, X-ray photoelectron spectroscopy (XPS), and temperature-programmed reduction by H(2) (H(2)-TPR). V/Fe-PILCs showed better catalytic performance than Fe-PILC without any significant SO(2) emissions. The H(2)S conversion over V/Fe-PILCs increased with increasing vanadia content up to 7 wt.%. However, it decreased at higher vanadia loading due to the decrease in surface area and the formation of the crystalline V(2)O(5) phase. The presence of water vapor in the reactant mixture resulted in a decrease of H(2)S conversion.     

On the Role of Vanadia Species for VOx／SiO2 in the Selective Oxidation of Methane

Various VOx/SiO2 catalysts were prepared by the methods of physical mixing, conventional wetness impregnation and ultrasonication-assistant impregnation. The catalysts were characterized by XRD, UV-Vis DRS, Raman, TPR, ESR and TPSR techniques and the nature of the vanadium species were correlated to their catalytic performance in the reaction of direct conversion of methane to formaldehyde. It is concluded that highly dispersed monomeric and low oligomeric vanadia species are formed on the sample prepared with both traditional wetness impregnation method and ultrasonication-assistant impregnation, whereas in the latter case, the amount of oligomeric vanadia species is much smaller. The V2O5 microcrystallines are the dominant species on the material prepared by physical mixing method. During the selective oxidation of methane, Vv species are reduced to V^IV paramagnetic species and both microcrystalline V205 species and oligomeric vanadia species are found to further disperse and transform into tetrahedral vanadia species. Based on the results of UV Raman spectroscopy and TPSR, C02 is suggested to be formed via two different routes, in which one is from the sequence reaction of CH4→ HCHO→ CO → CO2 over monomeric vanadia species, and the other is from the direct oxidation of methane to CO2 over oligomeric vanadia species. Oligomeric vanadia species is more active than monomeric vanadia species for methane activation.     

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.     

Dispersion state and catalytic properties of vanadia species on the surface of V_2O_5/TiO_2 catalysts

The dispersion state and catalytic properties of anatase-supported vanadia species are studied by means of X-ray diffraction (XRD), laser Raman spectroscopy (LRS), H2 temperature-programmed reduction (TPR) and the selective oxidation of o-xylene to phthalic anhydride. The almost identical values of the experimental dispersion capacity of V2O5 on anatase and the surface vacant sites available on the preferentially exposed (001) plane of anatase suggest that the highly dispersed vanadium cations are bonded to the vacant sites on the surface of anatase as derived by the incorporation model. When the loading amount of V2O5 is far below its dispersion capacity, the dispersed vanadia species might mainly consist of isolated VOx species bridging to the surface through V-O-Ti bonds. With the increase of V2O5 loading the isolated vanadia species interact with their nearest neighbors (either isolated or polymerized vanadia) through bridging V-O-V at the expenses of V-O-Ti bonds, resulting in the increase of the ra     

Catalytic Performance of Graphite Oxide Supported Au Nanoparticles in Aerobic Oxidation of Benzyl Alcohol: Support Effect

Various Au/GO catalysts were prepared by depositing Au nanoparticles on thermally- and chemically-treated graphite oxide (GO) supports using a sol-immobilization method. The surface chemistry and structure of GO supports were characterized by a series of analytical techniques including X-ray photoelectron spectroscopy, temperature-programmed desorption and Raman spectroscopy. The results show that thermal and chemical treatments have large influence on the presence of surface oxygenated groups and the crystalline structure of GO supports. A strong support effect was observed on the catalytic activity of Au/GO catalysts in the liquid phase aerobic oxidation of benzyl alcohol. Compared to the amount and the type of surface oxygen functional groups, the ordered structure of GO supports may play a more important role in determining the catalytic performance of Au/GO catalysts.     

介孔氧化铝负载钒催化剂上丙烷氧化脱氢制丙烯

 采用浸渍法制备了介孔氧化铝 (m-Al2O3) 负载钒催化剂 (V/m-Al2O3), 并考察了其催化丙烷氧化脱氢制丙烯反应活性. 通过 N2 吸附-脱附、透射电镜、X 射线粉末衍射、紫外-可见漫反射光谱、氢-程序升温还原和氨-程序升温脱附对催化剂进行了表征. 结果表明, 介孔氧化铝具有大比表面积、窄孔径分布和两维六方相结构, 在其上负载适量的 V 可实现 V 活性物种的高分散及催化剂的弱酸性, 从而有利于提高丙烷转化率和丙烯选择性. 与共合成法制备的含 V 介孔氧化铝 V/m-Al2O3(C) 和浸渍法制备的 V/?-Al2O3 相比, V/m-Al2O3 表现出更高的催化活性. 这与载体较弱的酸性和较大的比表面积以及 V 物种的高分散有关.     

V_2O_5/CeO_2催化剂上甲醇氧化一步法合成二甲氧基甲烷

采用溶胶-凝胶法制备了V2O5/CeO2催化剂,并用于甲醇氧化一步法合成二甲氧基甲烷(DMM)反应中.考察了V2O5含量对钒氧化物的存在状态、催化剂表面酸性、氧化-还原性及其催化甲醇氧化反应性能的影响.结果表明,V2O5含量为15%时钒氧化物呈单层分散,小于15%时以孤立或聚合态存在,大于20%时出现V2O5晶体,达到30%时出现CeVO4.当V2O5含量为15%时,较高的钒氧化物分散度使催化剂具有较强的氧化还原能力和较多的酸性中心,从而使催化剂具有较高的活性和DMM选择性.     

On the structure of vanadium oxide supported on aluminas: UV and visible raman spectroscopy, UV-visible diffuse reflectance spectroscopy, and temperature-programmed reduction studies

Vanadia species on aluminas (delta- and gamma-Al2O3) with surface VOx density in the range 0.01-14.2 V/nm2 have been characterized by UV and visible Raman spectroscopy, UV-visible diffuse reflectance spectroscopy (UV-Vis DRS), and temperature-programmed reduction in hydrogen. It is shown that the alumina phase has little influence on the structure and reducibility of surface VOx species under either dehydrated or hydrated conditions. Three similar types of dispersed VOx species, i.e., monovanadates, polyvanadates, and V2O5, are identified on both aluminas under dehydrated conditions. Upon hydration, polymerized VOx species dominate on the surfaces of the two aluminas. The broad Raman band at around 910 cm(-1), observed on dehydrated V/delta-, gamma-Al2O3 at all V loadings (0.01-14.2 V/nm2), is assigned to the interface mode (V-O-Al) instead of the conventionally assigned V-O-V bond. The direct observation of the interface bond is of significance for the understanding of redox catalysis because this bond has been considered to be the key site in oxidation reactions catalyzed by supported vanadia. Two types of frequency shifts of the V=O stretching band (1013-1035 cm(-1)) have been observed in the Raman spectra of V/Al2O3: a shift as a function of surface VOx density and a shift as a function of excitation wavelength. The shift of the V=O band to higher wavenumbers with increasing surface VOx density is due to the change of VOx structure. The V=O stretching band in dispersed vanadia always appears at lower wavenumber in UV Raman spectra than in visible Raman spectra for the same V/Al2O3 sample. This shift is explained by selective resonance enhancement according to the UV-Vis DRS results. It implies that UV Raman has higher sensitivity to isolated and less polymerized VOx species while visible Raman is more sensitive to highly polymerized VOx species and crystalline V2O5. These results show that a multiwavelength excitation approach provides a more complete structural characterization of supported VOx catalysts.     

双溶剂浸渍法制备VOX/MCF催化剂及丙烷选择氧化

采用双溶剂法制备了负载型氧化钒类催化剂(VOx/MCF),N2物理吸附、X射线衍射、透射电镜、拉曼光谱、程序升温脱附、程序升温还原等系统研究了催化剂的物化性质并测试了其在丙烷选择氧化反应中的催化性能.结果表明,由双溶剂法制备的VOx/MCF催化剂具有较好的催化活性,且在氧化钒负载量基本一致的前提下,双溶剂法制备的VOx/MCF催化剂比普通浸渍法制备的VOx/MCF具有更高的催化活性,这与双溶剂法的制备过程可以使得钒物种尽可能进入载体内表面,有利于氧化钒的较好分散有关,而高度分散的氧化钒物种,正是丙烷选择氧化反应的活性中心.     

富氮空心蠕虫状碳材料的合成及其苯甲醇非金属选择性催化氧化的高活性

Carbon materials have become one of the research hotspots in the field of catalysis as a typical representative of non-metallic catalytic materials. Herein, a facile synthetic strategy is developed to fabricate a series of hollow carbon nanoworms (h-NCNWs) that contain nitrogen up to 9.83 wt% by employing graphitic carbon nitride (g-C₃N₄) as the sacrificing template and solid nitrogen source. The h-NCNWs catalysts were characterized by X-ray diffraction (XRD), high-resolution transmission electron microscope (HR-TEM), N₂ adsorption-desorption, Fourier transform infrared spectroscopy (FT-IR), thermal gravimetric (TG), Raman spectra, and X-ray photoelectron spectroscopies (XPS). The catalytic activities of the h-NCNWs catalysts for selective oxidation of benzyl alcohol with O₂ were also evaluated. The characterization results revealed that the h-NCNWs catalysts displayed a unique hollow worm-like nanostructure with turbostratic carbon shells. The nitrogen content and shell thickness can be tuned by varying the relative ratio of resorcinol to g-C₃N₄ during the preparation process. Furthermore, nitrogen is incorporated to the carbon network in the form of graphite (predominantly) and pyridine, which is critical for the enhancement of the catalytic activity of carbon catalysts for the selective oxidation of benzyl alcohol. At a reaction temperature of 120 ℃, a 24.9% conversion of benzyl alcohol with > 99% selectivity to benzaldehyde can be achieved on the h-NCNWs catalyst prepared with a mass ratio of resorcinol to g-C₃N₄ of 0.5. However, the catalytic activities of the h-NCNWs catalysts were dependent on the amount of N dopants, in particular graphitic nitrogen species. The conversion of benzyl alcohol markedly decreased to 13.1% on the h-NCNWs catalyst prepared with a mass ratio of resorcinol to g-C₃N₄ of 1.5. Moreover, the h-NCNWs catalyst showed excellent stability during the reaction process. The conversion of benzyl alcohol and the high selectivity to aldehyde can be kept within five catalytic runs over the h-NCNWs0.5 catalyst. These results indicate that rationally designed carbon materials have great potential as highly efficient heterogeneous catalysts for oxidation reactions.     

Zn取代的磷钨酸季铵盐无溶剂氧化苯甲醇合成苯甲醛

合成了一系列过渡金属Zn取代的Keggin型磷钨杂多酸的季铵盐,采用傅里叶变换红外光谱(FTIR)、X射线衍射(XRD)等方法表征了杂多化合物的结构.并将其用于苯甲醇无溶剂氧化合成苯甲醛的反应,考察了催化剂种类、反应条件对苯甲醇氧化的影响.实验结果表明,在无任何溶剂的情况下,Zn取代的Keggin型磷钨四丁基铵盐具有最佳的催化活性,反应时间仅为30 min,苯甲醇的转化率可以达到95.6%,苯甲醛的选择性达到了96.4%.在对杂多酸季铵盐结构的研究基础上,对可能的反应机理进行了初步探讨.     

Influence of ceria modification on the properties of TiO2-ZrO2 supported V2O5 catalysts for selective catalytic reduction of NO by NH3

TiO(2)-ZrO(2) (hereafter denoted as Ti-Zr) supported V(2)O(5) catalysts with different loadings of CeO(2) were synthesized, and their physicochemical properties were characterized by Brunauer-Emmett-Teller (BET), X-ray diffraction (XRD), in situ Fourier transform infrared spectroscopy (in situ FT-IR) and temperature-programmed reduction (TPR). Their catalytic activities toward the NO(x) reduction reaction with NH(3) were tested. We found that with the addition of CeO(2), more NO was removed in a wide temperature range of 220-500 °C. As the CeO(2) content was increased from 10% to 20% (i.e., the molar ratio of Ce to Ti-Zr), NO conversion increased significantly; after that, increasing CeO(2) content, however, decreased NO conversion. In particular, the addition of CeO(2) to V(2)O(5)/Ti-Zr suppressed the coke deposition and rendered a stable and high catalytic activity. The characterization results indicated that: (1) the deposited vanadium and cerium oxides were highly dispersed over the Ti-Zr support, and in addition to ZrV(2)O(7), a common binary compound observed in V(2)O(5)/Ti-Zr, CeVO(4) and Ce(3)ZrO(8) was formed upon increasing CeO(2) content; (2) the introduction of CeO(2) to V(2)O(5)/Ti-Zr sample promoted the redox ability of the resulting catalysts; and (3) the Ce-containing catalysts possessed the greater amount of surface acidic and active intermediate.     

Ag/SBA-15低温气相选择性催化氧化苯甲醇合成苯甲醛

以SBA-15为载体,采用浸渍法制备了不同Ag含量的Ag/SBA-15,通过N₂吸附-脱附、X射线衍射、扫描电子显微镜、高分辨透射电子显微镜、X射线光电子能谱和电感耦合等离子体质谱对催化剂进行了表征。将Ag/SBA-15用于苯甲醇气相选择性催化氧化合成苯甲醛,研究了反应条件对转化率和选择性的影响。结果表明,Ag/SBA-15具有均一的一维孔道结构、较厚的孔壁（3-5 nm）及较大的比表面积（411-541 m²/g）,其规整纳米空间的限域作用使一定负载量的Ag以纳米尺寸均匀分散于介孔SBA-15孔道内,增加了活性组分的比表面积。亲核性氧物种从Ag到SBA-15表面的氧溢流,提高了低温下Ag/SBA-15对苯甲醇气相选择性氧化合成苯甲醛的催化性能。5.3% Ag/SBA-15中的Ag粒径为5-6 nm,且均匀分散于载体孔道中,反应温度为220℃时,苯甲醇转化率为87%,苯甲醛选择性为95%;240℃时,苯甲醇转化率和苯甲醛选择性分别高达94%和97%;并在240-300℃范围内,其催化活性和选择性保持不变,表现出了良好的温度耐受能力。催化剂经活化再生可以连续使用40 h,选择性基本保持不变。     

CeO2分散度对Au/CeO2-SiO2催化剂上甲醛的催化氧化影响

采用浸渍法在高比表面积的SiO2上负载不同量的CeO2,得到了CeO2不同颗粒尺寸的CeO2-SiO2载体,并用沉积沉淀法制备了CeO2-SiO2负载的纳米金催化剂.通过元素分析、X射线衍射、程序升温还原、N2物理吸附、拉曼光谱和透射电镜等技术对催化剂进行了表征,并考察了催化甲醛氧化活性.结果表明,高分散度、小尺寸的CeO2有利于得到较小尺寸的Au颗粒,并增强了催化剂的还原能力和氧缺位浓度,从而有利于提高催化剂低温甲醛催化氧化活性.     

CeO2纳米层对多层载体x-CeO2/3DOM Al2O3负载纳米Au催化剂催化柴油炭烟燃烧活性的影响

与汽油车相比,柴油车具有CO2排放低、寿命长和经济性好等优点,所以近年来受到广泛关注并被大量使用.但是,柴油车在使用过程中会产生大量炭烟颗粒物(PM),对大气环境和人类健康造成很大威胁.因此,开展这方面的基础研究具有重要的科学意义及环境保护意义.催化柴油炭烟燃烧反应是一个气-固-固多相深度氧化反应,由于PM的粒径远大于传统催化剂,导致PM不能进入催化剂孔道内部,造成催化剂活性比表面积利用率较低.设计并制备大孔径的三维有序大孔结构(3DOM)的催化剂,能够减小反应扩散阻力,增加催化剂与炭烟颗粒物的有效接触,加快反应进行.另外,可以通过在3DOM氧化物表面担载其它活性组分,提高催化剂的氧化还原性能,进而提高其活性.CeO2有很好的储放氧性能,在柴油车尾气净化催化剂中较为常见,但是单一的CeO2热稳定性较差,高温下容易烧结,使得比表面积减小,并且失去储氧能力,造成催化剂失活.文献中较常见的解决办法是在CeO2中掺杂其它阳离子,如Zr4+,Pr3+,Al3+,La3+及Y3+等离子,以提高CeO2的抗高温烧结能力.此外,研究报道的催化剂对催化柴油炭烟颗粒物燃烧的峰值温度已经远低于炭烟颗粒物的自燃温度,但是对颗粒物的起燃温度仍普遍较高.我们前期研究结果表明,担载纳米Au颗粒催化剂能够显著降低炭烟燃烧的起燃温度.本文采用胶体晶体模板法制备了3DOM Al2O3载体,利用微孔膜-氨沉淀法担载不同量的活性组分CeO2,制备出一种负载型x-CeO2/3DOM Al2O3催化剂,它既可减少稀土元素用量,降低成本,又因为Al2O3的机械强度较高,还能保证催化剂的机械强度足够好.为了进一步降低催化剂催化炭烟燃烧的起燃温度,利用还原沉积法在多层载体x-CeO2/3DOM Al2O3上负载纳米Au催化剂,制备出不同厚度的CeO2纳米层负载Au催化剂(Au/x-CeO2/3DOM Al2O3).利用X射线衍射、扫描电镜、透射电镜、H2程序升温还原和O2程序升温脱附等方法研究了催化剂的结构及物化性质与催化剂活性之间的关系,提出了消除PM反应的可能机理.结果表明,Al3+离子能够部分进入到CeO2中,形成Al-Ce固溶体.由于Al离子半径小于Ce离子,Al3+掺杂后能引起CeO2晶格发生畸变,产生大量缺陷,形成大量氧空位,促进晶格氧的移动,从而使催化剂具有更大的储放氧能力.在Au/x-CeO2/3DOM Al2O3催化剂中,CeO2担载量过高时,氧化铈纳米层较厚,活性组分容易烧结,不利于催化剂活性提高;而CeO2担载量过低,则CeO2纳米层较稀薄,催化剂的氧化还原性能受限,催化剂活性也不高.因此,CeO2的担载量应适当.此外,Au和CeO2之间的强相互作用能够增加Au纳米颗粒表面活性氧物种的数量,从而促进柴油炭烟燃烧反应.活性测试结果表明,担载纳米Au颗粒后,催化剂催化柴油炭烟燃烧的起燃温度均明显降低,在所制备的系列催化剂中Au/20％CeO2/3DOM Al2O3催化剂展示了最高的催化活性,T10,T50和T90分别为267,372和426 oC.     

Pt/CeO2-ZrO2-La2O3柴油车尾气氧化催化剂活性及抗硫性能

采用两种方法制备了三种Pt/CeO2-ZrO2-La2O3柴油车尾气氧化催化剂,并用X射线衍射、N2物理吸附、程序升温还原、程序升温脱附、X射线荧光光谱和红外光谱等方法对其进行了表征.结果发现,制备方法对催化剂的结构、织构、抗硫性能及催化性能的影响非常大.对其进行硫中毒,导致起燃温度明显升高.将ZrO2和La2O3沉积...