Quantitative Raman and ESCA characterization of titania supported tungsten catalysts

Summary The distribution of supported species in a series of W/TiO₂ catalysts (1.8 – 28 wt% WO₃) has been determined by Raman and X-ray photoelectron spectroscopy (XPS, ESCA). The results show that three tungsten species are present on oxidic W/TiO₂ catalysts. A tungsten interaction species is formed almost exclusively for catalysts with W loadings lower or equal to 6.7 wt% WO₃. WO₃ is observed above 6.7 wt% WO₃. For W loadings higher than 10 wt%, a disordered W species W_DS is also present. The amounts of W_DS and WO₃ increase with increasing W content above 10 wt% WO₃.Dedicated to Professor Dr. Wilhelm Fresenius on the occasion of his 80th birthday     

WOx/ZrO2 catalysts prepared by anionic exchange: in situ Raman investigation from the precursor solutions to the calcined catalysts

W/ZrO(2) catalysts were prepared using anionic exchange of peroxotungstate species with hydroxyl groups of zirconium hydroxide at low pH. The solids were dried and calcined under air at 700 degrees C. Each step of this novel method of preparation was investigated by Raman spectroscopy. A reference sample was also prepared by incipient wetness impregnation of ZrO(2).n(H2O) with an ammonium tungstate solution and characterized throughout its preparation process. Complementary data were collected from X-ray diffraction, chemical analysis, surface area measurements, and thermal analysis. The Raman spectra of the H2WO4-H2O2 precursor solutions evidenced the presence of (W2O3(O2)4(H2O)2)(2-) dimers. These low-nuclearity species were exchanged with zirconium hydroxide at low pH. The Raman spectra of the dried solids did not reveal peroxotungstate species but were typical of tetrahedral (WO4)(2-) species. A slight agglomeration of W species was observed with an increase in the W content. However, for an equivalent W loading, a higher W dispersion was obtained by anionic exchange, compared to the impregnation method. Furthermore, a remarkable homogeneity of the exchanged samples was evidenced by the micro-Raman spectra. The in situ Raman spectra recorded during calcination characterized both crystalline phases and supported tungsten species. Significant modifications were observed during the calcination process. The exchanged and the impregnated samples, with the same W loading, evidenced a similar type of tungsten species with one W=O bond. However, their behavior during calcination up to 700 degrees C was different. This was attributed to different strengths of interaction with the support. Moreover, the spectra recorded after calcination on various points of the exchanged sample with a high W content revealed a better spatial homogeneity than the impregnated one.     

Correlations between acidity, surface structure, and catalytic activity of niobium oxide supported on zirconia

The development of the acidity and the relationship between acidity, catalytic activity, and the surface structure for niobium oxide supported on zirconia were investigated for a series of solids. The catalysts were active for 2-propanol dehydration only above a threshold in Nb loading. The acidity was studied by infrared spectroscopy of adsorbed 2,6-dimethylpyridine as a probe molecule, and the onset of activity was correlated with that of the formation of relatively strong Br?nsted acid sites. The variation in the abundance of these sites also correlated with the catalytic activity. Raman, IR, and UV spectroscopy results indicated that the active sites were related to polymeric Nb surface species. These results were compared to those previously reported for the WO(x)/ZrO(2) catalysts.     

Fe柱撑海泡石负载Cu催化剂：结构特点及其C3H6选择性催化还原NO催化性质

通过羟基铁离子柱撑将海泡石(Sep)改性成Fe柱撑海泡石(Fe-PILSEP),使用浸渍法(IM)将Cu负载在Fe-PILSEP上,制得不同铜含量的xCu/Fe-PILSEP催化剂。通过X射线衍射(XRD)、N2-吸附/脱附、H2-程序升温还原(TPR)和X射线光电子能谱(XPS)等对样品进行表征,并测定其对丙烯选择性催化还原NO的催化活性。N2-吸附/脱附和TGA结果表明,Fe-PILSEP的比表面积和孔体积较海泡石原矿Sep极大地增加,热稳定性也明显优于Sep。XRD和XPS结果表明,在xCu/Fe-PILSEP催化剂上同时存在Fe3+/Fe2+和Cu2+/Cu+不同氧化态的氧化物,而且Fe与海泡石之间存在相互作用,Fe和Cu之间存在电子迁移。H2-TPR结果表明,xCu/Fe-PILSEP催化剂上存在不同聚集状态的氧化铜物种。xCu/Fe-PILSEP催化剂的丙烯选择性催化还原NO的催化活性明显优于Fe-PILSEP催化剂,这可能与Fe和Cu的氧化还原性有关。xCu/Fe-PILSEP的催化活性与Cu负载量相关,其中10Cu/Fe-PILSEP催化剂显示出最高的活性,这与其高的比表面积、孔体积和氧化还原性能,及其具有更多有利于HC-SCR反应的孤立Cu2+((Cu2+)i)物种有关。     

溶液pH值及钨前驱体影响含钨过氧物种结构的Raman光谱研究

识别水溶液体系中含过渡金属W ,Mo的过氧物种结构是探索烯烃、醇及醛等与双氧水催化选择氧化反应机理的关键所在 ,本研究借助高灵敏度的共焦显微Raman光谱表征手段 ,考察了Na2 WO4,(NH4) 10 [H2 W12 O42 ]和H3 PW12 O40 三种含钨前驱体在不同pH值条件下与过量双氧水作用产生的主要过氧物种的结构特征 ,推测在酸性较强 (pH <2 3 )的条件下三者产生的主要过氧物种结构相同 ,可能是单核式的 [WO2 (O2 ) 2 (H2 O) ] 2 -,而二聚态或多聚态的过氧物种几乎不存在于体系中 ;此外 ,还首次建立了通过Raman光谱来半定量测定双氧水浓度的分析方法 ,并尝试用于双氧水催化分解的动力学研究中 .     

WO3对MnOx/TiO2低温脱硝SCR催化剂的改性研究

以醋酸锰为前驱物通过浸渍法制备了MnO_x/TiO₂催化剂,用WO₃对载体进行改性制得一系列MnO_x-WO₃/ TiO₂催化剂,采用X射线衍射（XRD）、比表面积测定(BET)、拉曼光谱(LRS)、原位红外(FT-IR)光谱等表征技术进行相关的微观表征分析,同时在模拟氨气选择性催化还原NO_x（NH₃-SCR）的反应条件下对催化剂的脱硝反应活性进行了考察。研究表明,添加5%的WO₃拓展了载体的比表面积,提高了催化剂的抗热性,增加了催化剂表面的Brnsted酸位,拓宽其选择性催化还原脱硝活性温度窗口,对MnO_x/TiO₂催化剂有很好的改性作用;先钨后锰的负载顺序优于先锰后钨;随着温度的升高,化学催化反应速率提高,催化剂表面NH₃吸附峰呈减弱或消失趋势,故催化剂脱硝活性温度曲线呈中间高、两头低。     

钨含量对W/SiO2/Al2O3催化剂上1-丁烯自歧化反应的影响

采用浸渍法制备了一系列钨负载量不同的W/SiO₂/Al₂O₃ 催化剂. 采用X 射线衍射(XRD)、激光拉曼(Raman)光谱、紫外-可见(UV-Vis)光谱、氢气程序升温还原(H₂-TPR)和氨程序升温脱附(NH₃-TPD)等技术对催化剂进行了表征. 实验结果表明: 钨的负载量对催化剂上氧化钨物种的分散程度、还原性以及催化剂的酸性有非常重要的影响. 对该类催化剂上1-丁烯自歧化反应进行了详细考察, 结果表明: 当钨的质量分数为6.0%时,W/SiO₂/Al₂O₃催化剂表现出最佳的歧化活性和稳定性. 原因在于6.0%的钨负载量可以使催化剂上氧化钨物种具有中等程度的分散性、合适的还原性, 并且使催化剂具有一定程度的酸性, 这些因素有利于在催化剂上形成烯烃歧化活性位.     

新型WO3/TiO2纳米管催化剂的合成及其在环戊烯选择氧化反应中的性能研究

采用水热合成法以P25为原料制备了介孔TiO2纳米管, 并根据TEM和XPS表征结果对其形成机理进行了初步分析. 然后, 以制备出的介孔TiO2纳米管为载体, 钨酸铵为钨源, 采用传统浸渍方法制备了介孔WO3/TiO2纳米管催化剂. 利用N2吸附, TEM, XRD, XPS及Raman等手段对固载后的多相催化剂进行了表征, 并研究了催化剂在环戊烯选择氧化制备戊二醛反应中的催化性能. 结果表明, 在介孔20% WO3/TiO2纳米管催化下环戊烯的转化率达97.9%, 戊二醛的选择性高达69.3%. 钨物种以高度分散状态存在于催化剂中, 并与载体间存在着较强的相互作用, 使得钨的溶脱量很小, 脱落的钨对反应几乎没有影响. 另外, 催化剂具有较高的稳定性, 可以重复套用7次. 失活后的催化剂可通过简单焙烧的方式再生.     

Characterization of CuO supported on tetragonal ZrO2 catalysts for N2O decomposition to N2

A series of tetragonal zirconia-supported CuO oxide catalysts with various CuO loadings were characterized by X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), electron spin resonance (ESR), ultraviolet and visible diffuse reflectance spectroscopy (UV/vis-DRS), and temperature-programmed reduction (TPR) measurements. The results indicate that the dispersion capacity of copper oxide on this support is approximately 8.6 Cu(2+) ions/nm(2) ZrO(2). The state of the resulting supported copper species depends on the CuO loading. At CuO loadings below the dispersion capacity, only highly dispersed copper ion species are present on the surface of t-ZrO(2). In particular, isolated Cu ions are the predominant species at low loadings. In contrast, pair Cu ions become the most abundant species at loadings near the dispersion capacity. It has been proposed that these dispersed CuO (isolated and paired Cu ions) have a symmetric 5-fold-oxygen-coordination symmetry (C(3)(v) symmetry) and can be described as distorted octahedra with a missing corner or a trigonal bipyramids. Finally, at CuO loadings above the dispersion capacity the formation of crystalline CuO is observed. TPR results reveal that the dispersed Cu ion species have a different reducibility from CuO crystallites, presumably due to strong interactions between these species and the t-ZrO(2) support. The catalytic activity of these CuO/t-ZrO(2) catalysts for the decomposition of N(2)O can also be directly correlated to CuO dispersion, with paired Cu ions being the most active species for this reaction.     

低温陈化法制备SO_4~(2-)/WO_3-TiO_2固体超强酸及性能研究

0引言固体超强酸的研制是近20年来催化领域中的热点研究课题之一。起初,人们所研制的SO42-/MxOy型固体超强酸中,MxOy多为ZrO2。近年来,研究者们为得到高酸强度和高催化活性的固体超强酸催化剂,以ZrO2为主体,引入第二组分、第三组分组成复合型催化剂,这方面的研究者颇多[1~4],也     

Relations between structure, acidity, and activity of WOx/TiO2: influence of the initial state of the support, titanium oxyhydroxide, or titanium oxide

Two series of WO(x)/TiO(2) catalysts, containing W surface densities up to 4.4 W atoms/nm(2), were prepared by pore volume impregnation of two different supports, titanium oxyhydroxide (amorphous) or titanium oxide (crystallized, 100% anatase). The influence of W surface density and the nature of the support on the surface structure, development of the acidity, and catalytic performances were examined. The texture and structure of the catalysts were investigated by Brunauer-Emmett-Teller measurements, X-ray diffraction (XRD), and Raman and infrared spectroscopy. The catalytic activity was tested for 2-propanol dehydration and n-hexane isomerization. For catalysts obtained by impregnation of titanium oxide, XRD and Raman results showed that W was present as a surface phase. Infrared spectra indicated an increase in the degree of polymerization of W species with increasing W surface density. CO and lutidine adsorption, followed by infrared spectroscopy, showed an increase in the strength and abundance of Br?nsted acid sites (measured after lutidine desorption at 573 K) with the W surface density above a threshold of 1.3 W atoms/nm(2). The development of Br?nsted acidity correlated with the evolution of the infrared bands attributed to polymerized W species. A direct relationship was observed between the concentration of Br?nsted acid sites and the catalytic activity for 2-propanol dehydration. Catalytic activity, for n-hexane isomerization, appears to be associated with the presence of highly condensed W species. The catalysts synthesized by impregnation of titanium oxyhydroxide exhibited a comparable behavior. Hence, for a given W surface density, the W surface structure, concentration of Br?nsted acid sites, and catalytic performances were similar. Thus, no significant effect of the initial form of the support (titanium oxyhydroxide versus titanium oxide; 100% anatase) was evidenced.     

Atom-economy Synthesis of N-Substituted Carbamate from Urea Derivative and Dimethyl Carbonate Catalyzed by La/SiO_2: Characterization and Activity

A series of silica gel immobilized lanthanum catalysts were prepared for the atom‐economy synthesis of N‐substituted carbamates from urea derivatives and dimethyl carbonate. The La/SiO₂ catalysts with lanthanum loadings varied from 1.3 wt% to 8.5 wt% were characterized by AES, BET, XRD, TEM, FT‐IR, XPS and TPD. According to the characterization, lanthanum species with particle sizes of 5–10 nm on the surface of silica gel were formed. The catalysts were all amorphous and the surface areas were 336.5–530.2 m²/g. NH₃‐TPD analysis showed that all samples exhibited similar acid strength with different acid amounts. FT‐IR measurement indicated that the component of lanthanum species on the catalyst surface were La(OH)₃, LaOOH and hydrated La₂O₃. Also, the peak value of the absolute amount of LaOOH was obtained with 4.3 wt% lanthanum loading. The BET surface area decreased dramatically when the lanthanum loading was above 4.3 wt%. In consideration of the results obtained from the catalytic reactions, it could be concluded that LaOOH was the possible active species and high surface area was important for the high catalytic activity.     

Measurement of the surface coverage of V/Al2O3 catalysts by infrared spectroscopy,CO2 chemisorption and ion scattering spectroscopy

Quantitative FTIR studies of alumina hydroxyl groups have been used to measure the surface coverage of V/Al₂O₃ catalysts. The IR spectra show a preferential consumption of the most basic hydroxyls (3769 cm^?1) with the initial V uptake. The integrated area of the hydroxyl region was used to calculate the surface coverage of the catalysts. The surface coverage increased to 0.63 as the V loading increased to 6.7 wt%. The surface coverage results obtained from IR were compared to those measured by ion scattering spectroscopy (ISS) and CO₂ chemisorption. The surface coverages measured by ISS were comparable to those obtained by IR. In contrast, CO₂ chemisorption appears to overestimate the surface coverage of the catalysts. The overestimation of the surface coverage by the CO₂ chemisorption method is attributed to the preferential adsorption of the V phase onto the most basic hydroxyls, the same sites which interact with CO₂.     

Structural studies of high dispersion H3PW12O40/SiO2 solid acid catalysts

Highly dispersed H(3)PW(12)O(40)/SiO(2) catalysts with loadings between 3.6 and 62.5 wt% have been synthesised and characterised. The formation of a chemically distinct interfacial HPW species is identified by XPS, attributed to pertubation of W atoms within the Keggin cage in direct contact with the SiO(2) surface. EXAFS confirms the Keggin unit remains intact for all loadings, while NH(3) adsorption calorimetery reveals the acid strength >0.14 monolayers of HPW is loading invariant with initial DeltaH(ads) = approximately -164 kJ mol(-1). Lower loading catalysts exhibit weaker acidity which is attributed to an inability of highly dispersed clusters to form crystalline water. For reactions involving non-polar hydrocarbons the interfacial species where the accessible tungstate is highest confer the greatest reactivity, while polar chemistry is favoured by higher loadings which can take advantage of the H(3)PW(12)O(40) pseudo-liquid phase available within supported multilayers.     

Li-Mn/WO_(3)/TiO_(2)固体酸催化剂的制备及其甲烷氧化偶联催化性能研究北大核心CSCD

Li-Mn/WO_(3)/TiO_(2)催化剂具有良好的低温OCM催化性能,采用浸渍法制备Li-Mn/WO_(3)/TiO_(2)催化剂,并详细考察WO_(3)对催化剂物理化学性质及催化性能的影响.利用X射线衍射(XRD)、CO_(2)程序升温脱附(CO_(2)-TPD)、O_(2)程序升温脱附(O_(2)-TPD)、H_(2)程序升温还原(H_(2)-TPR)、拉曼光谱(Raman)和X射线光电子能谱(XPS)等表征技术对催化剂进行了研究,发现WO_(3)的添加提高了C_(2)选择性,并有效抑制了深度氧化.XRD与CO_(2)-TPD结果表明,WO_(3)的添加不仅有利于金红石型TiO_(2)的形成而且能够中和催化剂表面的强碱位,从而抑制了深度氧化反应.O_(2)-TPD和H_(2)-TPR结果表明,WO_(3)的添加降低了晶格氧(O^(2-))移动性,进而提高了反应的C_(2)选择性.此外,WO_(3)的添加促使了低温氧化偶联活性物种MnTiO_(3)的形成并提高了活性物种的分散性,因此提高了催化剂甲烷氧化偶联的反应活性和选择性.所有Li-Mn/x%WO_(3)/TiO_(2)催化剂中,Li-Mn/5%WO_(3)/TiO_(2)催化剂显示出最佳的OCM反应性能.在750℃,CH_(4)∶O_(2)∶N_(2)=10∶4∶5,GHSV=2280 mL·g^(-1)·h^(-1)条件下,最高的C_(2)产物收率可达16.3%.     

Measurement of the surface coverage of V/Al2O3 catalysts by infrared spectroscopy, CO2 chemisorption and ion scattering spectroscopy

Quantitative FTIR studies of alumina hydroxyl groups have been used to measure the surface coverage of V/Al₂O₃ catalysts. The IR spectra show a preferential consumption of the most basic hydroxyls (3769 cm^–1) with the initial V uptake. The integrated area of the hydroxyl region was used to calculate the surface coverage of the catalysts. The surface coverage increased to 0.63 as the V loading increased to 6.7 wt%. The surface coverage results obtained from IR were compared to those measured by ion scattering spectroscopy (ISS) and CO₂ chemisorption. The surface coverages measured by ISS were comparable to those obtained by IR. In contrast, CO₂ chemisorption appears to overestimate the surface coverage of the catalysts. The overestimation of the surface coverage by the CO₂ chemisorption method is attributed to the preferential adsorption of the V phase onto the most basic hydroxyls, the same sites which interact with CO₂.Dedicated to Professor Dr. Dieter Klockow on the occasion of his 60th birthday     

Na-W-Mn/SiO_2催化剂中Na对甲烷氧化偶联制乙烯的作用(英文)

采用常规浸渍法制备了一系列Na（wt％）含量不同的Na－W－Mn／SiO_2催化剂,在流动态微型固定床常压反应装置上评价了这些催化剂的甲烷氧化偶联（OCM）制乙烯催化反应性能,并进行了XPS、XRD表征。实验结果表明,Na含量为0．39wt％－2．34Wt％的Na－W－Mn／SiO_2催化剂具有好的甲烷氧化偶联制乙烯性能,此时Mn以对反应有利的晶相存在,同时由于Na的表面富集,引起W、Mn向催化剂表面发生迁移。由此可见,在Na－W－Mn／SiO_2催化剂中,Na是甲烷转化和乙烯生成不可缺少的活性组分之一。     

Quantitative determination of the speciation of surface vanadium oxides and their catalytic activity

A quantitative method based on UV-vis diffuse reflectance spectroscopy (DRS) was developed that allows determination of the fraction of monomeric and polymeric VO(x) species that are present in vanadate materials. This new quantitative method allows determination of the distribution of monomeric and polymeric surface VO(x) species present in dehydrated supported V(2)O(5)/SiO(2), V(2)O(5)/Al(2)O(3), and V(2)O(5)/ZrO(2) catalysts below monolayer surface coverage when V(2)O(5) nanoparticles are not present. Isolated surface VO(x) species are exclusively present at low surface vanadia coverage on all the dehydrated oxide supports. However, polymeric surface VO(x) species are also present on the dehydrated Al(2)O(3) and ZrO(2) supports at intermediate surface coverage and the polymeric chains are the dominant surface vanadia species at monolayer surface coverage. The propane oxidative dehydrogenation (ODH) turnover frequency (TOF) values are essentially indistinguishable for the isolated and polymeric surface VO(x) species on the same oxide support, and are also not affected by the Br?nsted acidity or reducibility of the surface VO(x) species. The propane ODH TOF, however, varies by more than an order of magnitude with the specific oxide support (ZrO(2) > Al(2)O(3) > SiO(2)) for both the isolated and polymeric surface VO(x) species. These new findings reveal that the support cation is a potent ligand that directly influences the reactivity of the bridging V-O-support bond, the catalytic active site, by controlling its basic character with the support electronegativity. These new fundamental insights about polymerization extent of surface vanadia species on SiO(2), Al(2)O(3), and ZrO(2) are also applicable to other supported vanadia catalysts (e.g., CeO(2), TiO(2), Nb(2)O(5)) as well as other supported metal oxide (e.g., CrO(3), MoO(3), WO(3)) catalyst systems.     

焙烧温度对柴油车氧化催化剂Pt-Pd-（x）ZrO2/Ce0.3Zr0.7O2-Al2O3性能的影响

制备了氧化铝、铈锆固溶体复合氧化物负载铂、钯的双金属催化剂Pt-Pd/ Ce0.3Zr0.7O2-Al2O3,并添加3% ZrO2助剂改性,用于柴油车尾气中CO、HC和NO的催化氧化,其中贵金属负载量仅为0.68 wt%。考察了制备过程中焙烧温度对催化剂性能的影响。催化剂活性评价结果表明,与未添加ZrO2的催化剂比较。添加ZrO2明显提高了催化剂的低温氧化活性,而且焙烧温度对催化剂的氧化性能有较大影响。焙烧温度为800 ?C时,CO和C3H6的起燃温度最低,分别为168、189 ?C,焙烧温度为700 ?C时,NO转化为NO2的转化率最高,最大转化率为36%,具有较好的热稳定性。通过XRD、N2吸附-脱附、CO化学吸附、XPS、H2-TPR等表征手段考察了催化剂物理化学性质随焙烧温度的变化情况,并分析了与催化剂活性之间的关系,得到贵金属分散度、表面化学吸附氧含量、催化剂的还原性质对氧化性能有重要影响,发挥协同作用。进而可以通过优化焙烧温度提升柴油车氧化催化剂性能,对提高工业应用柴油车尾气后处理系统的净化效率有重要意义。     

整体式Mn-Fe/ZrO2-TiO2催化剂的制备及在低温NH3-SCR反应中的性能

以锆钛复合氧化物为载体, 制备整体式Mn基催化剂并研究其在低温氨选择性催化还原(NH3-SCR)氮氧化物反应中的性能; 用BET、XRD、储氧量(OSC)、程序升温还原(TPR)和XPS对催化剂进行表征. 实验结果表明, 与以TiO2为载体的催化剂相比, 以ZrO2-TiO2为载体的催化剂具有较大的比表面积、更稳定的晶相结构和较多的储氧量, 并具有较强的低温氧化性能和较高的表面Mn含量, 表现出良好的低温活性和高温稳定性. 在700 ℃焙烧后, Mn-Fe/ZrO2-TiO2在高空速55000 h-1条件下, 仍具有较好的起燃温度(182 ℃)和NO的转化率(78%), 并具有较强的抗水性能, 表现出很好的应用前景.