Effects of the thermal decomposition of surface oxygen species on the chemical and catalytic properties of activated carbon supported Pt catalysts

Several carbon supported Pt catalysts were prepared by varying surface properties of support and tested for methylene chloride oxidation. They were investigated by BET, TPD, pH analysis and XPS. The Pt species would stabilize when the surface carbon was pregraphitized due to the π sites of basal plane. This revised version was published online in June 2006 with corrections to the Cover Date.     

MnOx/Al2O3/Ce0.45Zr0.45M0.10Oy （M = Mn, Y, La） catalysts used for ethanol catalytic combustion

MnOx/Al2O3/Ce0.45Zr0.45M0.10Oy (M = Mn,Y,La) catalysts were prepared by impregnation method and characterized by BET,TPR and XRD analyses.The catalytic activities toward ethanol combustion were investigated in a microreactor.The results demonstrated that the catalytic activity of MnOx/Al2O3/Ce0.50Zr0.50O2 monolithic catalyst could be improved by doping Mn,Y and La into Ce0.50Zr0.50O2.When doping Y into Ce0.50Zr0.50O2,the catalyst MnOx/Al2O3/Ce0.45Zr0.45Y0.10O1.95 showed the highest activity.The 100% conversion temperature of ethanol was 230 ℃.Furthermore,once the conversion of ethanol started,the complete conversion was quickly achieved.The doping of Mn,Y and La led to better activity for ethanol combustion and lower temperature reduction peaks in TPR profiles.The doping of Mn resulted in enhanced oxygen storage capacity (OSC),larger area of the reduction peaks,and excellent reactivity,and the doping of Y resulted in the lowest reduction temperature and the best activity.     

钴铝复合氧化物负载金催化剂的制备及催化分解N2O

分别用离子交换法和共沉淀法制备了钴铝复合氧化物负载金催化剂,用于催化分解N₂O。离子交换法制备的催化剂活性优于共沉淀法制备的催化剂。对于离子交换法制备的催化剂,考察了金负载量、HAuCl₄溶液的预处理方式、焙烧温度对催化剂活性的影响,用BET、XRD、H₂-TPR等技术对催化剂进行了表征,优化出了催化剂的最佳制备参数：金负载量1.1%、预调节HAuCl₄溶液的pH值至9.0、300℃焙烧。在钴铝氧化物中加入适量的助剂Na,提高了Co³⁺的还原性和催化剂的低温活性,在此基础上制备的1.5%Na/1.1%Au/Co-Al催化剂的低温活性优于1.1%Au/Co-Al和1.5%Na/Co-Al。     

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.     

Geometric stability of PtFe/PdFe embedded in graphene and catalytic activity for CO oxidation

The direct methanol fuel cell (DMFC) is considered as a promising power source, because of its abundant fuel source, high energy density and environmental friendliness. Among DMFC anode materials, Pt and Pt group metals are considered to be the best electrocatalysts. The combination of Pt with some specific transition metal can reduce the cost and improve the tolerance toward CO poisoning of pure Pt catalysts. In this paper, the geometric stabilities of PtFe/PdFe atoms anchored in graphene sheet and catalytic CO oxidation properties were investigated using the density functional theory method. The results show that the Pt (Pd) and Fe atoms can replace C atoms in graphene sheet. The CO oxidation reaction by molecular O₂ on PtFe–graphene and PdFe–graphene was studied. The results show that the Eley–Rideal (ER) mechanism is expected over the Langmuir–Hinshelwood mechanism for CO oxidation on both PtFe–graphene and PdFe–graphene. Further, complete CO oxidation on PtFe–graphene and PdFe–graphene proceeds via a two‐step ER reaction: CO(gas) + O₂(ads) → CO₂(ads) + O(ads) and CO(gas) + O(ads) → CO₂(ads). Our results reveal that PtFe/PdFe commonly embedded in graphene can be used as a catalyst for CO oxidation. The microscopic mechanism of the CO oxidation reaction on the atomic catalysts was explored.     

MoCo/Y, MoNi/Y氮化物催化剂的结构和CH4+CO2重整反应性能

采用氨气还原法制备了NaY分子筛负载的MoCo/Y、MoNi／Y双组氮化物催化剂，用XRD和EXAFS方法征了样品的结构，并测定了其在CH4＋CO2重整反应中的活性，在氧化态时，MoCo/Y样品中主要存在CoMoO4和Co3O4两种物相，Mo的配位状态接近于CoMoO4，而Co的配位状态更接近于Co3O4，MoNi／Y样品中主要有NiMoO4和NiO两种物相，Mo的配位状态接近于MiMoO4，而Ni的配位状态可能是NiMoO4和NiO两种化合物中Ni配位状态的平均效果，Ni-Mo之间的朴素作用似乎比Co-Mo相对较强，在氮化态时，两种样品中Mo的配位状态较为相似，但即不同于MoO3，也不同于单组分γ－Mo2N.Co和Ni的配位状态都不同于各在氧化态下的状态，且都在相同的位置出现一个新强峰，这似乎表明MoCo和MoNi生成了结构相似的氮化物，在CH4＋CO2重整反应中，氮化态MoCO/Y和MoNi/Y的活性大大超过非负载单组分γ－Mo2N催化剂，其中MoNi/Y的活性相对更好一些，且活性随Ni含量增加而提高。     

WO3/MO2 (M = Zr, Sn, Ti) heterogeneous acid catalysts: Synthesis, study, and use in cumene hydroperoxide decomposition

Thirty (5–40)% WO₃/MO₂ (M = Zr, Ti, Sn), heterogeneous acidic catalysts have been synthesized by two methods, specifically, via homogeneous acid solutions and from solutions brought to pH 9 with ammonia, both followed by calcination at 600–900°C. The catalysts have been characterized by IR spectroscopy and scanning electron microscopy, and their aqueous washings have been analyzed. Their acidity has been determined by the thermal analysis of samples containing adsorbed pyridine, and in terms of the proton affinity scale. Catalytic activities have been compared for cumene hydroperoxide (CHP) decomposition at 40°C in cumene and acetone. For all M, the catalysts are one type and contain W in strongly and weakly bound states, the latter being a polyoxometalate that can be washed off. Both tungstate phases are active in acid catalysis. Brønsted acid sites with a broad strength distribution have been found. The strongest of them are heteropolyacid protons. The catalysts 30% WO₃/SnO₂ and 20% WO₃/ZrO₂ (in acetone) and 10–20% WO₃/TiO₂ (in cumene) are the most active in CHP decomposition, and their activity is not related to their total acidity. Phases containing W⁶⁺ that form during the high-temperature synthesis are responsible for the high acidity, and additional protons that may appear owing to W⁶⁺ reduction can play only a minor role.     

Energetics of the O-H bond and of intramolecular hydrogen bonding in HOC6H4C(O)Y (Y = H, CH3, CH2CH=CH2, C[triple bond]CH, CH2F, NH2, NHCH3, NO2, OH, OCH3, OCN, CN, F, Cl, SH, and SCH3) compounds

The energetics of the phenolic O-H bond in a series of 2- and 4-HOC 6H 4C(O)Y (Y = H, CH3, CH 2CH=CH2, C[triple bond]CH, CH2F, NH2, NHCH 3, NO2, OH, OCH3, OCN, CN, F, Cl, SH, and SCH3) compounds and of the intramolecular O...H hydrogen bond in 2-HOC 6H 4C(O)Y, was investigated by using a combination of experimental and theoretical methods. The standard molar enthalpies of formation of 2-hydroxybenzaldehyde (2HBA), 4-hydroxybenzaldehyde (4HBA), 2'-hydroxyacetophenone (2HAP), 2-hydroxybenzamide (2HBM), and 4-hydroxybenzamide (4HBM), at 298.15 K, were determined by micro- or macrocombustion calorimetry. The corresponding enthalpies of vaporization or sublimation were also measured by Calvet drop-calorimetry and Knudsen effusion measurements. The combination of the obtained experimental data led to Delta f H m (o)(2HBA, g) = -238.3 +/- 2.5 kJ.mol (-1), DeltafHm(o)(4HBA, g) = -220.3 +/- 2.0 kJ.mol(-1), Delta f H m (o)(2HAP, g) = -291.8 +/- 2.1 kJ.mol(-1), DeltafHm(o)(2HBM, g) = -304.8 +/- 1.5 kJ.mol (-1), and DeltafHm(o) (4HBM, g) = -278.4 +/- 2.4 kJ.mol (-1). These values, were used to assess the predictions of the B3LYP/6-31G(d,p), B3LYP/6-311+G(d,p), B3LYP/aug-cc-pVDZ, B3P86/6-31G(d,p), B3P86/6-311+G(d,p), B3P86/aug-cc-pVDZ, and CBS-QB3 methods, for the enthalpies of a series of isodesmic gas phase reactions. In general, the CBS-QB3 method was able to reproduce the experimental enthalpies of reaction within their uncertainties. The B3LYP/6-311+G(d,p) method, with a slightly poorer accuracy than the CBS-QB3 approach, achieved the best performance of the tested DFT models. It was further used to analyze the trends of the intramolecular O...H hydrogen bond in 2-HOC 6H 4C(O)Y evaluated by the ortho-para method and to compare the energetics of the phenolic O-H bond in 2- and 4-HOC 6H 4C(O)Y compounds. It was concluded that the O-H bond "strength" is systematically larger for 2-hydroxybenzoyl than for the corresponding 4-hydroxybenzoyl isomers mainly due to the presence of the intramolecular O...H hydrogen bond in the 2-isomers. The observed differences are, however, significantly dependent on the nature of the substituent Y, in particular, when an intramolecular H-bond can be present in the radical obtained upon cleavage of the O-H bond.     

Ni(Co)-W-B非晶态催化剂的制备和加氢脱氧性能研究

采用化学还原法制备出非晶态催化剂Ni-W-B和Co-W-B,用BET、XRD和XPS对催化剂进行表征分析,以对甲基苯酚为模型化合物研究了两种催化剂的加氢脱氧性能。结果表明,所制备的两种催化剂均为非晶态结构,两种催化剂在对甲基苯酚的加氢脱氧反应中都显示出较好的脱氧活性。在相对低温523 K下,Ni-W-B催化剂显示较高的加氢活性,转化率达到100.0%,对甲基环己醇的选择性为55.1%,脱氧选择性只有44.1%,而Co-W-B催化剂显示出较高的脱氧活性,脱氧选择性达到93.1%,这主要是由于催化剂的表面不同价态元素组成含量引起的。在573 K和4.0 MPa下,催化对甲基苯酚的加氢脱氧反应的转化率和脱氧选择性都能达到100%。     

Bildung und Charakterisierung von Oberflächenverbindungen in den Systemen (C6H5CH2)4M/γ-Al2O3 (M = Ti,Zr)

Formation and Characterization of Surface Compounds in the Systems (C₆H₅CH₂)₄M/γ-Al₂O₅ (M = Ti, Zr) By O-bridges anchored surface-compounds are formed by protolytic splitting off of benzyl groups if tetrabenzyltitanium and -zirconium are added to γ-alumina. These compounds contain the metal in different oxidation states in dependence on the carrier/substrate ratio and the density of OH groups on the alumina surface. The different kinds of surface compounds are discussed. Furthermore, the products formed by thermal decomposition and hydrogenolysis of the surface compounds were analysed. With regard to catalytic conversion reactions of hydrocarbons systems of the type (C₆H₅CH₂)₄M/Pt/γ-Al₂O₃were involved in the investigations.     

Formation of mixed aryl–, alkyl–lithium aggregates in the heteroatom assisted lithiation of α,α′-dialkyl substituted 1,3-bis[(dimethylamino)methyl]benzene

The heteroatom assisted lithiation of 1,3-bis[1-(dimethylamino)ethyl]benzene with n-BuLi afforded 2,6-bis[1-(dimethylamino)ethyl]phenyllithium. An X-ray crystal structure determination revealed a dimeric aggregate in which the four benzylic chiral centers are identical, pointing to stereoselective crystallization. In contrast, reaction of 1,3-bis[1-(dimethylamino)propyl]benzene with n-BuLi afforded a dimeric aggregate comprising the parent lithiated compound and n-BuLi in a 1:1 molar ratio. The four Li atoms and the four bridging carbon atoms are arranged in a unique ladder-type C–Li₂–C₂′–Li₂–C framework.     

Pt/Al2O3 and Pt/Ba?Al2O3 catalysts studied by temperature programmed desorption of oxygen: Evidence for a low temperature desorbing species

For fresh and aged Pt/Al₂O₃ catalysts, TPD of oxygen is fairly well related to the noble metal surface areas and to the catalytic activity in butane combustion, whereas for aged Pt/Ba−Al₂O₃ solids, the catalytic activity is still preserved despite a tremendous sintering of the metallic phase and seems to be connected to a surface barium superoxide.     

制备方法对MnOx-CeO2催化剂理化性质及低温NH3-SCR脱硝性能的影响

随着人们环保意识的增强,氮氧化物(NOx)的危害引起广泛关注.NOx作为首要的大气污染物之一,主要来源于以燃煤电厂为代表的固定源和以机动车为代表的移动源.它不仅能够导致酸雨和光化学烟雾,而且还是PM2.5的重要前驱体,严重危害人类健康和植物生长.因此,NOx的治理迫在眉睫.研究表明,氨选择性催化还原(NH3-SCR)技术是控制固定源NOx排放最经济有效的方法.商业化V2O5-WO3/TiO2和V2O5-MoO3/TiO2脱硝催化剂的最佳工作温度窗口为300?400℃.因此,NH3-SCR脱硝设施通常安装在除尘器和脱硫装置之前以满足最佳工作温度需要.然而,在这种情况下,脱硝催化剂容易因烟气中的飞灰和含硫化合物堵塞、中毒而失活.此外,对于老电厂增加脱硝设施的改造工程,在除尘器和脱硫装置之前没有足够的空间用于安装脱硝设施.因此,开发环境友好型低温NH3-SCR脱硝催化剂显得尤为重要,因为它可以直接安装在除尘器和脱硫装置之后,从而有效减缓脱硝催化剂失活,有利于改造工程的施工.研究表明,锰基催化剂由于其优异的氧化还原性能和氧迁移能力有利于氧化NO为NO2,促进反应沿着"快速NH3-SCR"途径进行,从而表现出优异的低温脱硝性能.然而,其N2选择性、抗水性能和工作温度窗口还有待改善.因此,开发既具有高催化活性又具有宽工作温度窗口、优异抗水性能以及理想N2选择性的低温脱硝催化剂仍是一个富有挑战性的课题.二氧化铈(CeO2)由于具有优异的氧化还原性能、良好的储/释氧能力、丰富的氧空位以及Ce4+/Ce3+的轻易切换而被广泛用于NH3-SCR反应.因此,将锰氧化物(MnOx)与CeO2相结合而制备的MnOx-CeO2催化剂可能会表现出优异的低温脱硝性能.而催化剂的理化性质和催化性能还强烈地依赖于其制备方法.因此,本文采用不同方法(机械混合法、浸渍法、水热法、共沉淀法以及溶胶-凝胶法)制备了一系列MnOx-CeO2催化剂用于低温NH3-SCR反应,并运用X射线衍射(XRD)、拉曼光谱(Raman)、氮气物理吸附、氢气程序升温还原(H2-TPR)、氨气程序升温脱附(NH3-TPD)、X射线光电子能谱(XPS)以及原位漫反射红外光谱(in situ DRIFTS)等表征技术对催化剂进行了系统分析.重点考察了制备方法对MnOx-CeO2催化剂理化性质和催化性能的影响.结果表明,低温脱硝性能有如下顺序:水热法>溶胶-凝胶法>共沉淀法>浸渍法>机械混合法.这与催化剂表面Ce3+和Mn4+含量、氧空位和表面吸附氧物种浓度以及酸量和酸强度顺序一致.这些性质都与MnOx和CeO2之间的电子相互作用(即Mn3++Ce4+?Mn4++Ce3+)密切相关.特别是水热法制备的MnOx-CeO2催化剂(MnCe-HTM)由于Mnn+掺入到CeO2晶格形成铈基固溶体(含Mn-O-Ce结构)以及水热过程中的高温高压环境加强了MnOx和CeO2之间的电子相互作用,从而表现出优异的理化性质、最佳的低温脱硝性能以及理想的抗水性能.     

Au/TiO2催化剂上非催化CO氧化反应中活性氧物种的生成和消除

在定量的瞬时产物分析(TAP)反应器中,于80 oC下采用CO脉冲和O2脉冲补充等方法,研究了高温(400 oC)焙烧的Au/TiO2催化剂上活性氧物种的移除反应活性,特别是活性氧物种的性质。以往的研究大多关注的是CO催化氧化反应中活性氧物种及其性质,在典型的反应条件下该物种的形成和消除是可逆的;而本研究表明,催化剂直接焙烧后就存在额外的氧物种;该物种对CO氧化反应也具有活性,但其在典型的反应条件下不生成或生成很少。基于此,讨论了Au/TiO2催化剂上CO氧化反应的机理,特别是不同活性氧物种的作用。     

NaBH4处理LaCuZnX(X=Zr、Al、Zr+Al)(类)钙钛矿型催化剂及其CO2加氢合成甲醇性能的研究

采用共沉淀法分别制备了不同F-T组分(Fe、Co、Ni)改性的KCuZrO_2催化剂,并用于催化CO加氢合成异丁醇。通过BET、XRD、TEM、XPS、H_2-TPR、CO-TPD以及in-situ DRIFTS对催化剂进行了表征。结果显示,F-T组分的加入促进了乙醇和丙醇的形成,但是对异丁醇选择性影响不同。结果表明,Fe促进了催化剂中各组分的分散,活性组分Cu在催化剂表面发生了富集,提高了H_2/CO活化吸附;另外,KFeCuZrO_2的催化剂表面含有较多的C_1物种,有利于乙醇和丙醇进一步发生β-加成反应得到异丁醇,而Co和Ni改性的催化剂上缺少足够的C_1物种,因此,异丁醇的选择性并未明显增加。Co的引入对催化剂结构以及Cu的分散影响不大,但是Co改性后催化剂性能有所下降,其原因是催化剂发生了失活;Ni添加后催化剂比表面积有所减小,且催化剂表面Cu/Zr物质的量比也降低到0.19,催化剂粒径增大,Cu-Zr之间相互作用减弱,异丁醇选择性降低。     

Effect of additive in feedstock on performance of Ag-MoO3/ZrO2 catalyst for propylene epoxidation by molecular oxygen

Summary The performance of the Ag-MoO₃/ZrO₂ catalyst for propylene epoxidation by molecular oxygen is influenced obviously by the composition of feedstock. As an additive in feedstock, the presence of organic chloride, CO₂, NO_x or H₂ at a suitable concentration can improve the catalytic performance of Ag-MoO₃/ZrO₂ catalyst for the propylene epoxidation.      

Methanesulfonates of high-valent metals: syntheses and structural features of MoO2(CH3SO3)2, UO2(CH3SO3)2, ReO3(CH3SO3), VO(CH3SO3)2, and V2O3(CH3SO3)4 and their thermal decomposition under N2 and O2 atmosphere

Oxide methanesulfonates of Mo, U, Re, and V have been prepared by reaction of MoO(3), UO(2)(CH(3)COO)(2)·2H(2)O, Re(2)O(7)(H(2)O)(2), and V(2)O(5) with CH(3)SO(3)H or mixtures thereof with its anhydride. These compounds are the first examples of solvent-free oxide methanesulfonates of these elements. MoO(2)(CH(3)SO(3))(2) (Pbca, a=1487.05(4), b=752.55(2), c=1549.61(5) pm, V=1.73414(9) nm(3), Z=8) contains [MoO(2)] moieties connected by [CH(3)SO(3)] ions to form layers parallel to (100). UO(2)(CH(3)SO(3))(2) (P2(1)/c, a=1320.4(1), b=1014.41(6), c=1533.7(1) pm, β=112.80(1)°, V=1.8937(3) nm(3), Z=8) consists of linear UO(2)(2+) ions coordinated by five [CH(3)SO(3)] ions, forming a layer structure. VO(CH(3)SO(3))(2) (P2(1)/c, a=1136.5(1), b=869.87(7), c=915.5(1) pm, β=113.66(1)°, V=0.8290(2) nm(3), Z=4) contains [VO] units connected by methanesulfonate anions to form corrugated layers parallel to (100). In ReO(3)(CH(3)SO(3)) (P1, a=574.0(1), b=1279.6(3), c=1641.9(3) pm, α=102.08(2), β=96.11(2), γ=99.04(2)°, V=1.1523(4) nm(3), Z=8) a chain structure exhibiting infinite O-[ReO(2)]-O-[ReO(2)]-O chains is formed. Each [ReO(2)]-O-[ReO(2)] unit is coordinated by two bidentate [CH(3)SO(3)] ions. V(2)O(3)(CH(3)SO(3))(4) (I2/a, a=1645.2(3), b=583.1(1), c=1670.2(3) pm, β=102.58(3), V=1.5637(5) pm(3), Z=4) adopts a chain structure, too, but contains discrete [VO]-O-[VO] moieties, each coordinated by two bidentate [CH(3)SO(3)] ligands. Additional methanesulfonate ions connect the [V(2)O(3)] groups along [001]. Thermal decomposition of the compounds was monitored under N(2) and O(2) atmosphere by thermogravimetric/differential thermal analysis and XRD measurements. Under N(2) the decomposition proceeds with reduction of the metal leading to the oxides MoO(2), U(3)O(7), V(4)O(7), and VO(2); for MoO(2)(CH(3)SO(3))(2), a small amount of MoS(2) is formed. If the thermal decomposition is carried out in a atmosphere of O(2) the oxides MoO(3) and V(2)O(5) are formed.     

负载金催化剂上CO氧化反应活性与金属氧化物载体中金属-氧结合能之间的关系

讨论了金属氧化物载体(MOx)对其负载纳米金催化剂(Au/MOx)上CO氧化反应的影响。采用典型的共沉淀法和沉积-沉淀法在完全相同的焙烧条件下制备了一系列MOx负载金催化剂,以CO氧化转化50%时的反应温度(T1/2)定量评价了MOx载体和Au/MOx催化剂的催化活性。进一步将MOx载体与相应Au/MOx催化剂的T1/2值之差对MOx载体的金属-氧结合能做曲线进行关联,发现二者呈明显的火山型关系。这一结果表明,采用具有适当金属-氧结合能(300–500 atom O)的MOx可大大提高沉积于其上的Au纳米颗粒的催化活性。     

Selective catalytic reduction of NO over metal oxide or noble metal-doped In2O3/Al2O3 catalysts by propene in the presence of oxygen

The activities of metal oxide CuO, SnO₂, CoO, Ag₂O, ZnO or noble metal Pt, Pd, Rh-doped In₂O₃/Al₂O₃ catalysts for selective catalytic reduction of NO by propene were investigated. The temperature windows for NO reduction over noble metal-doped In₂O₃/Al₂O₃ catalysts were shifted and broaden slightly compared with single component catalyst alone. This revised version was published online in June 2006 with corrections to the Cover Date.     

Sm~(3+)掺杂(Y,Tb)AG:Ce~(3+)荧光粉的制备及光谱性能

采用柠檬酸溶胶凝胶燃烧合成法制备了一系列组成的(Y,Tb)3Al5O12:Ce3+,Sm3+荧光粉。通过X射线衍射、荧光光谱研究了不同Sm3+离子共掺杂浓度下(Y,Tb)AG:Ce3+荧光粉的晶体结构及光致发光性能。Rietveld全图拟合(Rietveld method of wholepattern fitting)结果表明:掺杂后样品仍为纯立方石榴石相,随着Sm3+离子共掺杂浓度的增加,样品的晶胞参数增大。在467 nm激发下,激发能由Ce3+离子向Sm3+离子单向传递,从而在617nm处出现红光发射。Tb3+离子取代不利于Ce3+离子与Sm3+离子的能量传递,同时Ce3+离子受更强的晶体场作用及与O2-离子间增强的共价性使发射主峰红移,Sm3+掺杂的TAG:Ce体系中,激发能由敏化剂Ce3+离子向激活剂Sm3+离子的传递路径包括5d→4f2F5/2,7/2(Ce3+)和7F6→5D4(Tb3+)到4G5/2→6H7/2(Sm3+)两部分。