胶溶法制备镧-钡共稳定氧化铝的性能

以硝酸为胶溶剂, 两种拟薄水铝石为前驱体, 用胶溶法制备了镧-钡共稳定的氧化铝. 采用X 射线衍射(XRD)、表面分析仪(BET)、氨气程序升温脱附(NH3-TPD)和NO2程序升温脱附(NO2-TPD)技术对所制备的镧改性和镧钡共改性氧化铝的结构特性和表面性能进行了表征. XRD结果表明, 改性氧化铝在1273 K焙烧后均以γ-Al2O3相存在. 当BaO添加量达到14%(w)时, 有少量BaCO3生成. BET结果表明, 在1273 K下焙烧5 h后, 5%(w)La2O3稳定的氧化铝(Ba-0)和5%La2O3与8%BaO共同稳定的氧化铝(Ba-8)均具有较大的比表面积, 各种氧化铝的吸附等温线表明它们的孔形状均为狭缝型孔和瓶型孔, 孔径分布曲线表明, 仅有样品Ba-8的孔径分布较宽, 孔径为6-10 nm, 其它三种样品的孔径均集中在10 nm; NH3-TPD结果表明, 随着氧化钡添加量的逐渐增多, 氧化铝表面的酸量、酸强度逐步减少. NO2-TPD结果表明, 添加BaO后载体对NO2的吸附量增多, 随着BaO含量的增多, 体相Ba(NO3)2增多. 由于样品Ba-8同时具有很好的织构性质、适中的表面酸量和酸强度分布及NO2吸附脱附能力, 使得以它为载体的催化剂具有最好的催化性能,丙烷的起燃温度和完全转化温度分别为526 K和593 K.     

氧化铝载体和氧化钡助剂对钌基氨合成催化剂结构和性能的影响

采用不同来源γ-Al2O3(市售Al2O3-1,合成Al2O3-2)作为钌基氨合成催化剂载体,利用浸渍法制备了一系列添加不同BaO助剂含量的Ba-Ru/Al2O3催化剂.通过X射线衍射(XRD)、N2-低温物理吸附、X射线荧光光谱(XRF)、透射电镜(TEM)、H2程序升温还原(H2-TPR)、NH3程序升温脱附(NH3-TPD)和X射线光电子能谱(XPS)等方法研究了不同来源的Al2O3以及BaO助剂含量对负载型钌基催化剂的物相结构、织构性质、微观形貌、表面性质和催化剂的氨合成活性等方面的影响.结果表明,载体的物理化学性质对制备的钌基氨合成催化剂的结构以及活性有较大影响.BaO助剂对催化剂的影响主要表现在两个方面:添加量不同导致BaO与γ-Al2O3的作用力不同,从而进一步影响催化体系的比表面积和孔结构性质;BaO助剂会对体系的Ru物种还原性质以及催化剂表面酸碱性质进行调节,适量BaO的加入能够极大提高反应活性,而这种最佳量与载体性质密切相关.     

Pt/Ba-Al-O催化剂储存NOx的性能和机理研究

采用共沉淀法制备了Pt/Ba-Al-O样品.用XRD、 NO-TPD以及NOx储存量测量等手段对样品进行了表征, 并对NOx的储存机理进行了探讨.结果表明, 样品中的主要成分是BaAl2O4, 有少量BaCO3存在.在催化剂表面的Pt有两种吸附位,吸附位1为NO提供了吸附位,对应低温区的NO脱附峰;吸附位2使NO和O2在催化剂表面反应生成硝酸盐和亚硝酸盐,对应高温区的NO脱附峰.当吸附温度为300℃、 O2的体积分数为1.3%时, NO的脱附量达到了最大值.经过还原处理样品的NO吸附能力比经过氧化预处理的样品强得多.样品储存NOx的最佳温区为300～450℃.     

钙改性的Pd/CeO2-ZrO2-Al2O3催化剂催化甲醇裂解反应

采用共沉淀法制备了未改性的和Ca掺杂的CeO2-ZrO2-Al2O3样品,进一步用浸渍法制备了Pd/CeO2-ZrO2-Al2O3(Pd/CZA)和Pd/CeO2-ZrO2-Al2O3-CaO (Pd/CZACa)催化剂.运用X射线衍射、N2吸附-脱附、储氧量测定、CO化学吸附、NH3程序升温脱附、CO2程序升温脱附、...     

不同MgO担体对Ba-Ru/MgO氨合成催化剂物化性质和反应性能的影响

采用不同沉淀剂制备了MgO材料,以其为载体制备了Ba-Ru/MgO氨合成催化剂,考察了沉淀剂种类和BaO助剂对其氨合成性能的影响.通过X射线衍射(XRD)、N2物理吸附、X射线荧光光谱(XRF)、透射电镜(TEM)、H2程序升温还原(H2-TPR)、CO2程序升温脱附(CO2-TPD)、H2程序升温脱附(H2-TPD)和N2程序升温脱附(N2-TPD)表征手段,对不同沉淀剂影响Ba-Ru/MgO催化剂氨合成性能的原因进行了探索.结果表明:采用(NH4)2CO3作沉淀剂制备的Ba-Ru/MgO催化剂表面Ru物种易于在低温下还原,催化剂表面在低温区具有较多数量的弱碱性吸附位,在450℃、5.0 MPa和5 000 h-1条件下,由(NH4)2CO3做沉淀剂制备的Ba-Ru/MgO催化剂活性最高,出口氨浓度为3.74%.BaO助剂的加入大大减少了Ba-Ru/MgO催化剂表面吸附氢的数量,增大表面脱附氮的数量,从而易于N2解离吸附,提高氨合成反应速率.     

Pt/MOx-SiO2 (M=Ce,Zr, Al)催化剂对CO和C3H8氧化性能的影响

采用共沉淀法制备质量比为1:1的MOx-SiO2(M=Ce,Zr,Al)复合氧化物,以此为载体采用浸渍法制备了铂基氧化型催化剂.考察了该系列催化剂在模拟柴油车尾气条件下,经SO2硫化前后对C3H8和CO的氧化性能.用X射线衍射(XRD)、低温N2吸附-脱附、氨气/氧气/二氧化碳程序升温脱附(NH3/O2/CO2-TPD)和X射线光电子能谱(XPS)等手段进行了表征.NH3-TPD证实催化剂表面存在多种酸中心,硫化后催化剂表面中强酸中心增多.O2-TPD证实催化剂表面存在α和β氧物种,硫化后催化剂表面氧脱附量减少.其中Pt/Al2O3-SiO2表面酸性最弱和表面氧脱附量最大.XPS结果表明新鲜催化剂经硫化后会使催化剂表面Pt的结合能降低.活性测试结果表明,三种催化剂对CO和C3H8的催化氧化活性均较好,其中Pt/ZrO2-SiO2抗SO2中毒性能最佳,具有良好的应用前景.     

Pt/Ce0.75Zr0.25O2的催化性能及其氧移动性的 18O 同位素交换表征

 采用浸渍法制备了Pt/Ce0.75Zr0.25O2催化剂,考察了催化剂对乙醇及CO的氧化活性,并采用 18O 同位素交换、乙醇程序升温表面反应(C2H5OH-TPSR)、一氧化碳程序升温脱附(CO-TPD)和程序升温还原(H2-TPR)等技术对催化剂进行了表征. 结果表明, Pt/Ce0.75Zr0.25O2催化剂表现出较高的乙醇和CO氧化活性,其催化活性随着Pt负载量的增加而提高. 当Pt负载量为3%时,活性最高. 继续增加Pt负载量,催化剂活性下降. C2H5OH-TPSR和CO-TPD结果表明,催化剂对乙醇或CO的氧化活性与从催化剂表面脱附出来的CO2量有对应关系, CO2脱附量越大,催化剂活性越高. 18O 同位素交换结果表明,表面氧交换能力与其氧化活性有一定对应关系,催化剂的表面氧交换能力越高,氧化活性越高.     

MgO催化剂上以H2O2为氧源的苯乙烯环氧化反应

采用直接焙烧Mg(NO3)2·6H2O制备了固体MgO催化剂,并以H2O2为氧源,乙腈为溶剂,考察了其对苯乙烯环氧化反应的催化性能.运用X射线衍射、N2吸附-脱附、热重和CO2程序升温脱附对催化剂进行了表征.结果表明,MgO表面碱的强度在苯乙烯环氧化反应中起主导作用,而其表面的碱量、比表面积及孔体积等的影响较小.经75...     

研究NO在SrTiO3表面的吸附特性

采用TPD实验方法测定了N¹⁸O在SrTiO₃表面吸附后的脱附谱, 揭示了气体脱附量的变化规律. 结果表明N¹⁸O在SrTiO₃表面吸附后脱附出大量的N¹⁶O气体, 还脱附出少量的N₂, N¹⁸O和N₂¹⁶O气体. 这说明了在吸附和脱附过程中N¹⁸O与SrTiO₃表面发生氧的同位素交换. N¹⁶O的脱附量随N¹⁸O气体暴露量增加而增加, 但当气体覆盖度超过一定值后, 脱附量趋于定值.     

铁钼氧化物TPD-MS及催化性能的研究

制备了一系列不同配比的Ｆｅ－Ｍｏ氧化物催化剂,采用比表面积,ＸＲＤ,ＦＴ－ＩＲ和ＬＲＳ等方法,考察了催化剂的有关物化性质,测定了对甲苯选择性氧化生成苯甲醛的催化活性。用ＴＰＤ－ＭＳ技术研究了催化剂表面氧物种的脱附。结果表明,随着样品中Ｆｅ／Ｍｏ含量的改变,表面氧物种的脱附峰的峰温,氧脱附量和脱附活化能Ｅｄ也发生变化。３＃样品的氧脱附峰峰温较低,表面氧物种Ｏ＾－和Ｏ＾２－脱附量最大,Ｅｄ值最小,生成     

NO2 adsorption on BaO/Al2O3: the nature of nitrate species

Temperature programmed desorption, infrared spectroscopy, and (15)N solid state NMR spectroscopy were used to characterize the nature of the nitrate species formed on Al(2)O(3) and BaO/Al(2)O(3) NO(x) storage/reduction materials. Two distinctly different nitrate species were found: surface nitrates that are associated with a monolayer BaO on the alumina support, and a bulk-like nitrate that forms on this thin BaO layer. The surface nitrates desorb as NO(2) at lower temperatures than do the bulk-like nitrates, which decompose as NO+O(2) at higher temperatures. The amount of NO(x) stored in the monolayer nitrate is proportional to the surface area of the catalyst, while that in the bulk nitrate increases with BaO coverage.     

Ba deposition and oxidation on theta-Al2O3/NiAl(100) ultrathin films. Part II: O2(g) assisted Ba oxidation

Ba deposition on a theta-Al(2)O(3)/NiAl(100) substrate and its oxidation with gas-phase O(2) at various surface temperatures are investigated using X-ray photoelectron spectroscopy (XPS), Auger electron spectroscopy (AES), and temperature programmed desorption (TPD) techniques. Oxidation of metallic Ba by gas-phase O(2) at 800 K results in the growth of 2D and 3D BaO surface domains. Saturation of a metallic Ba layer deposited on theta-Al(2)O(3)/NiAl(100) with O(2)(g) at 300 K reveals the formation of BaO(2)-like surface states. These metastable peroxide (O(2)(2-)) states are converted to regular oxide (O(2-)) states at higher temperatures (800 K). In terms of thermal stability, BaO surface layers (theta(Ba) < 5 ML) that are formed by O(2)(g) assisted oxidation on the theta-Al(2)O(3)/NiAl(100) substrate are significantly more stable (with a desorption/decomposition temperature of c.a. 1050 K) than the thick (2 < theta(Ba) < 10 ML) metallic/partially oxidized Ba layers prepared in the absence of gas-phase O(2), whose multilayer desorption features appear as low as 700 K.     

Mechanisms for O2 dissociation over the BaO (100) surface

We have investigated the atomic and molecular oxygen adsorptions on the various sites of the BaO (100) surface with both cluster models and the periodic slab models. We found that the atomic oxygen prefers to adsorb on the surface O2- to form the closed-shell peroxides with the binding energies of 83-88 kcal/mol. Such a high exothermicity provides a large driving force for the dissociation of molecular O2 on the BaO surfaces. As molecular oxygen approaches the BaO surfaces, the triplet ground state O2 molecule first binds electrostatically on top of the surface Ba2+ site. It further quenches to the singlet potential energy surface to form a covalently bonded O3(2-) species. We proposed a plausible pathway in which the O3(2-) species acts as the key precursor for further dissociation, leading eventually to the formation of surface peroxides O2(2-). This mechanism is helpful for the understanding of a series of related catalytic processes such as the oxidative coupling of methane, the NOx storage reduction, etc.     

BaO对Pd/Al2O3催化性能的影响

以 Pd(C2 H3O2 ) 2 为前身 ,制备了系列 Ba O- Al2 O3复合氧化物负载钯的催化剂 .用质量滴定法 ,测定了复合载体的零电荷点 (pzc) .结果表明 ,体系的 pzc随 Ba O含量的增加而增大 ,在 5 %～ 10 %之间存在一拐点 ,并与XRD所测 Ba O在 Al2 O3上的单层分散阈值相对应 .复合载体在制备中发生固相反应 ,所生成的 Ba Al2 O4可以阻止 Al2 O3的相变 ,并极大地提高载体的热稳定性 ,其中 5 % Ba O的作用最为明显 .Ba O的引入 ,增强了 Pd/Al2 O3对 CO的氧化能力 ,同时 ,提高了其热稳定性     

高T~cYBa~2Cu~3O~7-xF~y超导体表面和体相的化学态的XPS研究

以NH~4F作为F^-源,制备了一系列不同含F量的高T~cYBa~2Cu~3O~7-xF~y超导体,在名义F含量小于1.5mol范围内,基T~c值均比与之对照的不含F样品高2～6K.用XPS研究了这类含F材料表面和体相的化学态及其变化,根据同种化合物中不同元素间的结合能差和其它辅助实验结果,标识了每个元素不同化学态的光电子峰,并对各个峰的可能来源及其对应原子在结构中的位置和作用进行了讨论.结果揭示,表现和体相的体学态存在着较大差异.     

Effect of barium on reducibility and activity for cobalt-based Fischer-Tropsch synthesis catalysts

Barium modified Co/Al2O3 catalysts were prepared by incipient wetness impregnation. The catalysts were characterized by XRD, TPD and DRIFTS. The catalytic activity for Fischer-Tropsch synthesis was measured in a continuously stirred tank reactor. It was found that small amounts of BaO (≤ 2 wt%) improved the cobalt reducibility, which led to more cobalt active sites on the catalyst surface, and then resulted in higher CO conversion and C5+ selectivity. However, for the catalysts with high BaO loadings negative effects on the catalytic activity and selectivity for high hydrocarbons were observed because of low cobalt reducibility.     

Isolation of two-dimensional 2:1 cation-ordered perovskite units by anion vacancy ordering in Ba6Na2Nb2P2O17

A new six-layer perovskite-related structure Ba 6Na 2Nb 2M 2O 17 (M = P, V), which consists of cubic (c) BaO 3 layers and oxygen-deficient pseudocubic (c') BaO 2 layers stacked in the sequence c'ccccc, is presented. In Ba 6Na 2Nb 2M 2O 17, two-dimensional slabs of the well-known 2:1 octahedral cation-ordered perovskite motif are isolated between layers of tetrahedral units formed by anion vacancy ordering: two consecutive NbO 6 octahedral layers are sandwiched by two single NaO 6 octahedral layers, which, in turn, connect with two isolated MO 4 tetrahedral layers. Both oxides are derived from the 2:1 ordered perovskite structure (e.g., Ba 3ZnTa 2O 9) by ordered removal of O atoms in every sixth BaO 3 layer. Both materials exhibit a relative permittivity of approximately 20-23, Q x f 0 values of approximately 7800-10600 GHz, and negative temperature coefficients of the resonant frequency of approximately -23 to -7 ppm/ degrees C.     

Water-induced morphology changes in BaO/gamma-Al2O3 NOx storage materials

Exposure of NO(2)-saturated BaO/gamma-Al(2)O(3) NO(x) storage materials to H(2)O vapour results in the conversion of surface nitrates to Ba(NO(3))(2) crystallites, causing dramatic morphological changes in the Ba-containing phase, demonstrating a role for water in affecting the NO(x) storage/reduction properties of these materials.     

Thermal Decomposition of BaC2O4·0.5H2O Studied by Stepwise Isothermal Analysis and Non-Isothermal Thermogravimetry

Thermal decomposition of BaC2O4·0.5H2O in air was studied by a combination of stepwise isothermal analysis (SIA) and non-isothermal thermogravimetry. The results from both techniques show that the crystal water is released in one step and that anhydrous barium oxalate is decomposed in one step, while BaCO3 decomposes in three steps to BaO, forming two intermediate compounds with the formulas of BaCO3·(BaO)2 and (BaCO3)0.5·(BaO)2.5. Reaction mechanism analyses using the data from SIA measurements show that the controlling mechanism for all the five decomposition steps in isothermal conditions is a two-dimensional phase-boundary controlled process. Kinetic parameters are obtained for the five decomposition steps from the non-isothermal thermogravimetric data. This revised version was published online in July 2006 with corrections to the Cover Date.