水分子在MoO3原子簇模型表面吸附的密度泛函研究

利用密度泛函理论(DFT)的B3LYP方法,在LANL2DZ基组上,计算了水分子吸附前后MoO3原子簇模型物的优化几何构型和电子结构,并进行了二级Mφller-Plesset微扰(MP2)相关能计算.结果表明,当水分子吸附于模型分子后,由于占据了MO5+空位,从原来留有空位的MoO5H4模型转变为MoO5H4·H2O模型的正八面体构型,水分子的氧通过占据在π键轨道中的电子向中心原子Mo的d轨道配位而被吸附,且水分子在模型物质表面呈吸附状态后,体系最稳定,能量最小,吸附过程不必翻越能垒,该过程放热91.39kJ/mol(MP2相关能校正),研究结果对催化剂的使用、失活和再生有较好的指导意义.     

Ag-MoO3催化丙烯直接气相环氧化反应的原位红外研究

制备了对丙烯直接气相环氧化具有较好催化性能的Ag-MoO3催化剂, 采用原位FT-IR技术研究了丙烯、环氧丙烷及丙烯+氧气的混合气在Ag和Ag-MoO3催化剂表面上的吸附及反应行为. 研究表明, 丙烯在Ag和Ag-MoO3催化剂表面上吸附后, 均不发生化学反应, 而环氧丙烷吸附后在较高温度下则发生开环和聚合反应直至产生积炭. 与Ag催化剂相比, 在Ag-MoO3催化剂上, MoO3的加入在降低催化剂活性的同时, 在一定程度上抑制了产物环氧丙烷的开环及深度反应, 使环氧丙烷的选择性提高. 另外, 在较低的反应温度和较短的滞留时间下, 环氧丙烷发生深度反应的程度明显降低.     

氧化铜表面臭氧分解路径及表面氧物种生成机理研究

基于密度泛函理论（DFT）计算研究了O3在完整和具有氧空位的CuO(111)表面吸附的吸附位、吸附结构、吸附能和电子转移情况,比较了O3在完整表面和具有氧空位的表面分解的路径和能垒,分析了氧空位和表面吸附氧的生成机理。结果表明,在完整CuO表面,O3分子通过化学吸附或物理吸附表面结合,吸附能最高为-1.22eV（构型bri(2)）。O3在具有氧空位的CuO表面均为化学吸附,吸附能最高为-2.95eV（构型ovbri(3)）,显著高于完整表面的吸附能。O3吸附后,Cu吸附位的电荷密度减小,O3中的O原子附近的电荷密度显著增强,电荷从CuO表面转移到O3,并形成Cu-O离子键。O3分解后形成了超氧物种,提高了表面的氧化活性。在完整表面,以构型bri(2)为起始构型的路径反应能垒最低,为0.52eV;O2*在完整表面的脱附所需要的最低能量为0.42eV,形成氧空位的O2*脱附能为2.06eV。在具有氧空位的表面,O3分解的反应能垒为0.30eV（构型ovbri(1)）和0.12eV（构型ovbri(3)）,均低于完整表面的反应能垒;分解形成的O2*的最低脱附能也低于完整表面,为0.27eV。可见,氧空位的形成提高了吸附能,降低了反应能垒,使O3分子更容易吸附在CuO表面,并加快了O3的催化分解。     

K_2O助剂对合成碳酸二甲酯用Cu-Ni/MoO_3-SiO_2催化剂吸附和反应性能的影响

用等体积浸渍法制备了MoO3 SiO2 (MoSiO)表面复合氧化物负载的Cu Ni K2 O催化剂。利用IR ,TPR ,TPD以及微反技术研究了K2 O助剂对CO2 和CH3OH在Cu Ni MoSiO催化剂表面上吸附和合成DMC(碳酸二甲酯 )反应性能的影响。结果表明 :K2 O助剂的加入 ,使CO2 在催化剂表面吸附强度增加 ,当K2 O含量达Cu Ni总量的 15 %时 ,CO2 在催化剂表面上吸附后生成K2 CO3;CH3OH在催化剂表面上的解离吸附态 (CH3O- H )的吸附强度减弱 ;CO2 和CH3OH在Cu Ni K2 O MoSiO催化剂表面反应主要产物为DMC ,H2 O ,CO和CH2 O。随着K2 O助剂的加入 ,反应转化率在 10 %之前增加 ,之后下降 ,DMC选择性稍有提高。副产物 (CO和CH2 O)的选择性下降。根据实验结果探讨了K2 O对催化剂表面活性中心的电荷分布的影响。     

WO3/ZrO2固体酸催化苯与1-己烯烷基化反应

 用浸渍法制备了WO3/ZrO2及碱金属K或碱土金属Sr掺杂改性的WO3/ZrO2固体酸催化剂. 采用X射线衍射、 N2吸附、 NH3程序升温脱附和吸附吡啶的红外光谱等技术表征了K或Sr对WO3/ZrO2催化剂结构和表面酸性质的影响. 研究了WO3/ZrO2及K或Sr掺杂改性的WO3/ZrO2固体酸对苯与1-己烯烷基化反应的催化性能. 考察了催化剂制备条件和反应条件对催化剂活性的影响以及催化剂的重复使用性. 结果表明,引入K或Sr可调变WO3/ZrO2固体酸中的ZrO2晶相和固体酸的酸强度、酸量以及Lewis酸中心与Brnsted酸中心的比值. 适量K或Sr掺杂改性可提高WO3/ZrO2催化剂对苯与1-己烯烷基化反应的催化活性和稳定性,在常压和80 ℃的温和条件下,反应10 min后, 1-己烯的转化率可达99%, 单烷基选择性为100%. 该催化剂可多次重复使用,催化活性稳定.     

H2在WO3表面解离吸附反应的第一性原理研究

采用第一性原理方法对H2在WO3表面的解离吸附反应进行了研究.首先通过清洁表面模型的计算,证明了c(2×2)重构表面是最稳定的WO3(001)表面构型;进而研究了4种可能的H2解离吸附模型,结果表明最可能的吸附反应为两个氢原子吸附在表面O1c原子上,氢原子被氧化在表面形成水,同时伴随着产生一个表面氧空位.态密度结果表明氢的吸附导致体系能带下移,导带部分填充电子,从而阐明了实验中WO3吸附H2后电导率上升的微观机理.     

Mo-HMS的制备及其催化丙烯液相环氧化反应性能

采用一步水热法合成了Mo-HMS催化剂,并用X射线衍射、N2吸附-脱附、透射电镜、激光拉曼光谱和紫外-可见光谱对催化剂的结构及表面钼物种进行了表征.结果表明,一步水热法可将Mo物种引入HMS载体中,而不破坏分子筛孔道结构,Mo物种在载体表面呈多种分布状态,包括单核的钼物种、聚集状态的多聚钼酸根离子(如Mo7O246)和晶相MoO3.与浸渍法制备的MoO3/HMS及溶胶-凝胶法制备的MoO3/SiO2相比,一步法可以使催化剂中MoO3晶相的含量分别下降39%和61%,在丙烯与异丙苯过氧化氢的环氧化反应中,Mo-HMS表现出最佳的催化性能.这可归结于Mo-HMS中Mo物种较高的分散度.     

K2O助剂对合成碳酸二甲酯用Cu—Ni／MoO3—SiO2催化剂吸附和反应性能的影响

用等体积浸渍法制备了MoO3-SiO2(MoSiO)表面复合氧化物负载的Cu-Ni-K2O催化剂。利用IR,TPR,TPD以及微反技术研究了K2O助剂对CO2和CH3OH在Cu-Ni/MoSiO催化剂表面上吸附和合成DMC（碳酸二甲酯）反应性能的影响。结果表明：K2O助剂的加入,使CO2在催化剂表面吸附强度增加,当K2O含量达Cu-Ni总量的15%时,CO2在催化剂表面上吸附后生成K2CO3;CH3OH在催化剂表面上的解离吸附态（CH3O^- H^ ）的吸附强度减弱;CO2和CH3OH和Cu-Ni-K2O/MoSiO催化剂表面反应主要产物为DMC,H2O,CO和CH2O。随着K2O助剂的加入,反应转化率在10%之前增加,之后下降,DMC选择性稍有提高。副产物（CO和CH2O）的选择性下降。根据实验结果探讨了K2O对催化剂表面活性中心的电荷分布的影响。     

CeO2表面分散态WO3的氨选择性催化还原性能

铈基材料在氨选择性催化还原氮氧化物(NH3-SCR)的研究中备受关注,亦被认为是潜在的新型环境友好型催化剂.CeO2具有独特的氧化还原性能和优良的储释氧性能,易与其它金属氧化物发生协同催化而有利于提高催化剂的催化反应性能,而WO3可以改善催化剂的表面酸性.研究亦报道了WO3可以改善CeO2的NH3-SCR反应的高温活性和N2选择性,其原因在于WO3增加了铈基催化剂NH3的吸附性能且抑制了NH3非选择性氧化成NOx.我们采用浸渍法制备了一系列负载型WO3/CeO2催化剂,并利用XRD,Raman,XPS,H2-TPR,NH3-TPD和in situ DRIFT对其理化性质进行了表征,系统研究了WO3负载量对WO3/CeO2催化剂NH3-SCR催化性能的影响,主要研究的内容包括:(1)WO3/CeO2催化剂中WO3的状态与催化性能之间的关系;(2)WO3负载量对WO3/CeO2催化剂的NH3和NO吸附行为的影响.NH3-SCR反应测试表明WO3负载量对WO3/CeO2催化剂有显著影响,优化的WO3/CeO2催化剂在200–450℃具有良好的脱硝性能,且在300℃通入SO2+H2O条件下依然保持优异的催化活性.XPS和H2-TPR结果表明,WO3分散在CeO2表面抑制了CeO2表面活性氧和表面晶格氧的氧化能力,这导致催化剂对NO的氧化以及对硝酸盐的吸附性能相比于纯CeO2显著降低,同时,in situ DRIFT也证实,随着WO3负载量的增加,WO3/CeO2催化剂表面吸附硝酸盐能力下降.因此,我们认为,由于低活性的晶相WO3覆盖在催化剂表面,阻碍了催化剂的表面活性位,降低了催化剂的氧化还原能力和表面酸量,从而晶相WO3抑制了WO3/CeO2催化剂的催化活性.同时,我们发现在70℃下采用氨水可以洗掉WO3/CeO2催化剂中的晶相WO3,且洗涤后的样品催化活性有所提升,这进一步验证了晶相WO3对催化活性的抑制作用.In situ DRIFT结果表明WO3/CeO2催化剂上NH3-SCR反应是通过Eley-Rideal机理进行,即吸附NH3物种与气相NO之间发生反应.随着WO3负载量的增加,WO3/CeO2催化剂中NH3的吸附能力先增强后减弱,而NO吸附能力持续减弱,这有利于表面酸位在反应过程中不被硝酸盐阻碍,当WO3负载量在分散容量附近时,这种吸附特性的效果发挥到最大,从而最大限度地促进NH3-SCR反应按照Eley-Rideal机理顺利进行.     

丙烯在Fe-Sb-W-O/SiO2催化剂上氧化机理的研究Ⅱ.吸附丙烯的程序升温脱附

用程序升温脱附技术研究了丙烯与铁锑氧化物催化剂之间的反应,结果表明该催化剂有两种不同结合强度的活性晶格氧和两种吸附丙烯中心,催化剂活性主要取决于表面晶格氧的活动性。比较了铁锑和钼系(C-41)两种氧化物催化剂上吸附丙烯后的程脱结果,并提出了丙烯在铁锑氧化物催化剂上的氧化机理。     

负载型三氧化钼催化剂表面结构和表面酸位的激光Raman光谱研究

测定了MoO3/γ-Al2O3、MoO3/TiO2、MoO3/SiO2的激光Raman谱. 通过MoO3/γ-Al2O3、MoO3/TiO2在吡啶吸附前后、氨水提取前后的谱图对比说明, 单层分散的MoO3, 即特征峰为～950cm^-^1的"二维聚钼酸"中钼的配位状态不是单一的,其中一种表面含钼物种(Mo-1)不吸附吡啶, 不溶于氨水, 不显示较强的表面酸性; 另一种表面含钼物种(Mo-2)可吸附吡啶, 溶于氨水, 与催化剂的表面酸位密切相关. 我们认为Mo-1为四面体配位的钼; Mo-2为八面体配位的钼. MoO3/SiO2中的MoO3能100%被氨水溶去, 其酸位数与表面Mo^6^+数之比接近1, 是由其中Mo-2的比例较高, 载体与活性组分之间的相互作用较弱这两个因素所造成的。     

Electronic structure and chemical bonding in MO(n)- and MO(n) clusters (M = Mo, W; n = 3-5): a photoelectron spectroscopy and ab initio study

Photoelectron spectroscopy (PES) and ab initio calculations are combined to investigate the electronic structure of MO(n)- clusters (M = W, Mo; n = 3-5). Similar PES spectra were observed between the W and Mo species. A large energy gap between the first and second PES bands was observed for MO3- and correlated with a stable closed-shell MO3 neutral cluster. The electron binding energies of MO4- increase significantly relative to those of MO3-, and there is also an abrupt spectral pattern change between MO3- and MO4-. Both MO4- and MO5- give PES features with extremely high electron binding energies (>5.0 eV) due to oxygen-2p-based orbitals. The experimental results are compared with extensive density functional and ab initio [CCSD(T)] calculations, which were performed to elucidate the electronic and structural evolution for the tungsten oxide clusters. WO3 is found to be a closed-shell, nonplanar molecule with C3v symmetry. WO4 is shown to have a triplet ground state (3A2) with D2d symmetry, whereas WO5 is found to be an unusual charge-transfer complex, (O2-)WO3+. WO4 and WO5 are shown to possess W-O* and O2-* radical characters, respectively.     

New luminescent solids in the Ln-W(Mo)-Te-O-(Cl) systems

Solid-state reactions of lanthanide(III) oxide (and/or lanthanide(III) oxychloride), MoO3 (or WO3), and TeO2 at high temperature lead to eight new luminescent compounds with four different types of structures, namely, Ln2(MoO4)(Te4O10) (Ln = Pr, Nd), La2(WO4)(Te3O7)2, Nd2W2Te2O13, and Ln5(MO4)(Te5O13)(TeO3)2Cl3 (Ln = Pr, Nd; M = Mo, W). The structures of Ln2(MoO4)(Te4O10) (Ln = Pr, Nd) feature a 3D network in which the MoO4 tetrahedra serve as bridges between two lanthanide(III) tellurite layers. La2(WO4)(Te3O7)2 features a triple-layer structure built of a [La2WO4]4+ layer sandwiched between two Te3O72- anionic layers. The structure of Nd2W2Te2O13 is a 3D network in which the W2O108- dimers were inserted in the large tunnels of the neodymium(III) tellurites. The structures of Ln5(MO4)(Te5O13)(TeO3)2Cl3 (Ln = Pr, Nd; M = Mo, W) feature a 3D network structure built of lanthanide(III) ions interconnected by bridging TeO32-, Te5O136-, and Cl- anions with the MO4 (M = Mo, W) tetrahedra capping on both sides of the Ln4 (Ln = Pr, Nd) clusters and the isolated Cl- anions occupying the large apertures of the structure. Luminescent studies indicate that Pr2(MoO4)(Te4O10) and Pr5(MO4)(Te5O13)(TeO3)2Cl3 (M = Mo, W) are able to emit blue, green, and red light, whereas Nd2(MoO4)(Te4O10), Nd2W2Te2O13, and Nd5(MO4)(Te5O13)(TeO3)2Cl3 (M = Mo, W) exhibit strong emission bands in the near-IR region.     

Mo-Co系加氢精制催化剂中TiO~2-Al~2O~3载体效应的PASCA研究

本文采用PASCA(化学分析正电子湮没谱)技术, 系统地研究了MoO~3/γ-Al~2O~3,CoO/γ-Al~2O~3, MoO~3/TiO~2-Al~2O~3, CoO/TiO~2-Al~2O~3等体系中活性组分的表面分散状态和化学状态及其变化规律, 揭示了用TiO~2改性Al~2O~3对Mo-Co系加氢精制催化剂所产生的载体效应的作用机理。Al~2O~3中引入TiO~2使得载体与MoO~3间的相互作用大大减弱, 导致分散态MoO~3易于还原和硫化。助剂CoO与TiO~2-Al~2O~3载体间存在极为显著的电子相互作用, 对于改善Co在活性相中的化学状态, 提高活性中心的内在活性具有重要的作用。PASCA研究的另一个重要结果是, 由于载体表面的不均匀性,使得上述负载型催化剂中氧化物活性组分的表面状态十分复杂, 存在与载体相互作用强弱程度不同的多类特征区, 这些特征区与内在活性不同的催化中心相关联. 通过TiO~2改性Al~2O~3载体, 有效地调节载体表面性质, 改变活性组分表面物种的分布及化学状态。     

Na(1.5)Ag(1.5)MO3F3 (M = Mo, W): an ordered oxyfluoride derivative of the LiNbO3 structure

Na(1.5)Ag(1.5)MoO(3)F(3) and Na(1.5)Ag(1.5)WO(3)F(3) have been synthesized by solid state reactions and structurally characterized using synchrotron X-ray and neutron powder diffraction. Unlike the vast majority of salts containing [MO(3)F(3)](3-) anions (M = Mo, W) the oxyfluoride groups in Na(1.5)Ag(1.5)MoO(3)F(3) and Na(1.5)Ag(1.5)WO(3)F(3) are orientationally ordered, so that the Na(+) ions are coordinated by fluorine and the Ag(+) ions by oxygen. The resulting structure type, which has not previously been reported, is related to the LiNbO(3) structure, but the combination of Na/Ag ordering and orientational ordering of the [MO(3)F(3)](3-) anions produces a supercell that doubles the c-axis and changes the space group symmetry from R3 to R3. The use of hard (Na(+)) and soft (Ag(+)) cations to direct the orientational ordering of polar oxyfluoride building units provides a new approach to the design of polar materials.     

Oxygen/sulfur substitution reactions of tetraoxometalates effected by electrophilic carbon and silicon reagents

Reactions of [MO(4)](2)(-) (M = Mo, W) with certain carbon and silicon electrophiles were investigated in acetonitrile in order to produce species of potential utility in the synthesis of analogues of the sites in the xanthine oxidoreductase enzyme family. Silylation of [MoO(4)](2)(-) affords [MoO(3)(OSiPh(3))](1)(-), which with Ph(3)SiSH is converted to [MoO(2)S(OSiPh(3))](1)(-). Reaction with (Ph(3)C)(PF(6))/HS(-) yields the tetrahedral monosulfido species [MO(3)S](2)(-), previously obtained only from the aqueous system [MO(4)](2)(-)/H(2)S. Dithiolene chelate rings are readily introduced upon reaction with 1,2-C(6)H(4)(SSiMe(3))(2), leading to the square pyramidal trioxo complexes [MO(3)(bdt)](2)(-), a previously unknown dithiolene molecular type. Further ring insertion occurs upon reaction of [WO(3)(bdt)](2)(-) with 1,2-C(6)H(4)(SSiMe(3))(2), giving [WO(2)(bdt)(2)](2)(-). Related reactions occur with [ReO(4)](1)(-). Treatment with 1 equiv of (Me(3)Si)(2)S produces [ReO(3)S](1)(-); with 3 equiv of 1,2-C(6)H(4)(SSiMe(3))(2), [ReO(bdt)(2)](1)(-) is obtained with concomitant Re(VII) --> Re(V) reduction. X-ray structures are reported for [MO(3)S](z)(-) (M = Mo, W, z = 2; M = Re, z = 1), [MO(3)(bdt)](2)(-), and [WO(2)(OSiPh(3))(bdt)](1)(-), a silylation product of [WO(3)(bdt)](2)(-). [MoO(3)(bdt)](2)(-) is related to the site of inactive sulfite oxidase, and [WO(2)(OSiPh(3))(bdt)](1)(-) should closely approximate the metric features of the [(dithiolene)MoO(2)(OH)] site in inactive aldehyde/xanthine oxidoreductase. This work provides convenient syntheses of known and new derivatives of tetraoxometalates, among which is entry to a unique class of oxo-monodithiolene complexes.     

Supported molybdena catalysts: Characterization of oxidized,reduced, and sulfided MoO3 prepared by an adsorption method

Highly dispersed molybdena-titania catalyst can be prepared by an equilibrium adsorption method. In this method, molybdate anions adsorb onto the positively charged titania surfaces via electrostatic attraction by controlling the pH of the impregnating solution and they increase as an inverse function of the pH. ⁹⁵Mo-NMR and UV spectroscopic studies of impregnating solution show that the polymeric species like Mo₇O₂₄ ⁶-ions are adsorbed on titania in the acidic impregnating solution. XRD, Raman, and XPS data of the calcined samples show that mono-layer coverage of molybdenum oxide over-layer possesses a highly distorted MoO₆ group with a molecular geometry resembling the distorted square pyramid. The catalytic oxidation of methanol over the surface molybdate species on titania possesses higher turnover numbers and higher selectivities of partial oxidation products than the catalysts supported on alumina, silica, zirconia, or magnesia. Changes of the surface properties either after reduction and sulfiding treatment over monolayer catalyst on titania have also been investigated. The NO chemisorption and XPS studies show that two types of active sites appeared after reduction treatment: one site is active for hydrogenation of 1,3-butadiene and the other site is active for metathesis of propene. A higher degree coordinative unsaturations of MO is required for hydrogenation than metathesis. After sulfiding treatments of the catalyst, hydrogenation of 1,3-butadiene also requires triply coordinative unsaturation, and hydrogenolysis of thiophene requires the ensemble of doubly or triply coordinative unsaturations.     

NaOH 改性WO_3/SiO_2 催化剂催化2-丁烯和乙烯复分解制丙烯(英文)

A WO3 /SiO2 catalyst is used in industry to produce propylene from 2-butene and ethylene metathe-sis. Catalysts with various WO3 loading(4% to 10%) were prepared by impregnation and tested for the metathesis of ethene and trans-2-butene. Ion exchange of NaOH onto the WO3/SiO2 catalyst was used to mitigate the acidity of the catalysts in a controlled way. At low WO3 loading, the treatment with large amounts of NaOH resulted in a significant decrease in metathesis activity concomitant with significant W leaching and marked structural changes(XRD, Raman). At higher WO3 loading (6% to 10%), the treatment with NaOH mainly resulted in a decrease in acidity. FT-IR experiments after adsorption of pyridine showed that the Lewis acidic sites were poisoned by sodium. Never-theless, the metathesis activity remained constant after the NaOH treatment. This suggested that the remaining acidity on the catalyst was enough to ensure the efficient formation of the carbene active sites. Interestingly, Na poisoning resulted in some modification of the selectivity. The mitigation of acidity was shown to favor propene selectivity over the formation of isomerization products (cis-2-butene, 1-butene, etc.). Moreover, treatment with NaOH led to a shorter induction period and reduced coke formation on the WO3 /SiO2 catalyst.     

Changes in surface composition of Fe-Si-Cr-K oxide alkylation catalyst: the marked role of potassium ferrites

The influence of gas-phase methylation of phenol on the state of the Fe-Si-Cr-K oxide catalyst surface was investigated by thermodesorption of K atoms and ions. Changes in potassium desorption energies, as determined from Arrhenius-like plots, varied from 3.07 eV to 1.21 eV for the atoms and from 2.59 eV to 2.89 eV for ion desorption from the active and deactivated samples, respectively. The results were discussed in terms of transformation of the catalyst surface and formation of β-ferrite.     

Adsorption of Propene on Neutral Gold Clusters in the Gas Phase

The adsorption of propene on neutral gold clusters is investigated in a collision cell under a few collision conditions. The adsorption reaction is studied by pressure‐dependent kinetic measurements and delayed unimolecular dissociation of the excited Au_n?propene complexes. The cluster size (n=9–25) and temperature (T=90–300 K) dependence of the propene adsorption is analyzed. Strong size dependences of the absorption reaction are observed; a larger propene adsorption probability was found for gold clusters composed of an even number of atoms. Propene binding energies are estimated by comparison of the temperature‐dependent unimolecular dissociation rates with rates obtained by using statistical RRKM modeling. The Au_n–propene binding energies decrease non‐monotonously with cluster size and are in the range of 1.2–0.85 eV for n=9–25. Finally, the bonding of C₃H₆ on Au_n is qualitatively described and similarities with the absorption of CO molecules on gold clusters are discussed.