铈和镧对Q345B钢在海洋大气中腐蚀行为的影响

通过周浸实验对普通Q345B钢和含有微量稀土铈(Ce)和镧(La)的Q345 BRE钢在模拟海洋大气腐蚀环境下,进行了耐腐蚀性能比较.利用失重和电化学方法进行两者的腐蚀速率比较,利用SEM和XRD分析了两者腐蚀形貌和锈层的特征.结果表明:加入混合稀土铈和镧的Q345B钢的腐蚀速率小于普通的Q345B钢,且腐蚀形貌也发生...     

Ba_3(PO_4)_2:Ce~(3+),Dy~(3+)荧光粉的组成与发光特性研究

在活性炭还原气氛下高温固相法合成了Ba3(PO4)2:Ce3+,Dy3+紫外发射荧光粉。XRD图谱表明,烧结温度为1100℃时保温处理3 h,样品为单相的Ba3(PO4)2型六方晶系结构。荧光光谱显示:单掺Ce3+样品中,Ce3+掺杂浓度为8%(摩尔分数)时样品的发光最强,发射峰的位置处在350 nm附近(Ce3+的2D→2F5/2和2D→2F7/2跃迁发射)。适量的Sr2+取代部分Ba2+离子,改变了基质晶格环境,使样品的发光强度得到提高且发射峰向长波方向红移。引入Dy3+作为敏化剂,样品发射峰红移到386 nm,亮度增强,主要是由于Dy3+和Ce3+之间发生了有效的能量传递过程。确定了Dy3+的最佳掺杂浓度为3%,发光强度提高了27%。     

Sm-Co/α-Fe/Sm-Co三层膜磁性能的微磁学模拟

以微磁学理论为基础,利用OOMMF软件采用三维动力学模型模拟研究了Sm-Co/α-Fe/Sm-Co交换耦合三层膜体系的磁滞回线,并对其磁性能分别与软、硬磁层厚度的关系进行了系统的分析.研究结果表明:只有当软磁层厚度小于其临界尺寸(5 nm)时,磁滞同线近似为矩形,此时三层膜完全耦合;硬磁层的厚度对体系的磁性能也有着密切的关系,而且硬磁层的厚度对体系软磁相的临界尺寸也有着一定的影响,只有在合适的软、硬磁含量比例的情况下才能得到具有最佳磁性能的三层膜.     

Ce-TiO_x超细粒子的模板法制备及结构研究

利用模板法结合真空干燥技术制备出Ce-TiOx超细粒子,用XRD,TG-DSC,TEM等手段进行表征;以甲基橙溶液的光催化降解测试Ce-TiOx超细粒子的催化活性;考察初始物质的量比及热处理温度对Ce-TiOx超细粒子的结构及光催化活性的影响。结果显示:钛干凝胶经400℃热处理可得结晶度较高的锐钛矿型TiO2,800℃时TiO2转变为金红石相;Ce-Ti干凝胶经800℃热处理可得粒径约为45 nm的类球形颗粒;Ce-TiOx超细粒子中,钛以Ti3O5,Ti6O11,TiO2等多种形式存在,铈以CeO2和Ce7O12的形式存在;稀土铈影响Ce-TiOx超细粒子中钛的价态。     

稀土Ce掺杂对ZnO结构和光催化性能的影响

采用共沉淀-焙烧法合成了一系列不同含量的稀土Ce掺杂的ZnO光催化剂. 利用傅里叶变换红外(FT-IR)光谱、粉末X射线衍射(XRD)、扫描电镜(SEM)、紫外-可见(UV-Vis)光谱、光致发光(PL)谱等技术对所制备的光催化剂进行了系列表征. 以酸性橙II脱色降解为模型反应, 考察了掺杂不同含量的铈及不同焙烧温度对ZnO的物理结构和光催化脱色性能的影响. 结果表明: 掺入质量分数(w)为2%的铈可以明显改善氧化锌表面状态, 有利于产生更多的表面羟基; 同时可以抑制光生电子与光生空穴(e^-/h⁺)的复合, 显著提高光催化脱色活性和光催化稳定性; 焙烧温度对光催化剂的晶体结构、表面性能和光催化活性产生较大影响, 500 °C的焙烧处理使样品的结晶度较高, 同时催化剂颗粒粒径较细, 表面具有丰富的羟基. 但过高的焙烧温度(600-800 °C)将导致催化剂的物理结构发生恶化, 降低光催化性能.     

Ce掺杂Mn3O4及其电化学电容行为

用溶胶-凝胶方法合成了Mn₃O₄和Ce掺杂Mn₃O₄. 采用X射线衍射(XRD)、傅里叶变换红外(FT-IR)光谱、场发射扫描电镜(FESEM)和透射电子显微镜(TEM)对其结构和形貌进行了表征. 采用循环伏安、电化学交流阻抗和恒流充放电技术对其电化学性能进行了测试. 研究结果表明, Ce掺杂对Mn₃O₄的形貌和电化学性能均有显著影响. 当Ce离子占金属离子总量的3%时, 掺杂Mn₃O₄的单电极比电容高达477 F·g^-1, 比未掺杂的提高了43.7%, 并且表现出更好的循环稳定性.     

Ti:Al2O3纳米粉体的共沉淀法合成及表征

本文采用共沉淀法合成了Ti:Al2O3纳米粉体.利用热重/差热(TG/DTA)/X射线衍射(XRD)/红外光谱(FTIR)/扫描电镜(SEM)以及能谱(EDS)等分析方法对合成的Ti:Al2O3纳米粉体进行了表征.结果分析表明:前驱体在1200℃下,保温1h可以得到纯的α-Al2O3晶相;粉体的粒径均匀、分散性好,平均粒径在25～50 nm之间.     

Synthesis and Crystal Structure of Rare Earth Metal Chlorides Bearing Bridged-Indenyl Ancillary Ligand

Two new rare earth metal chloride complexes supported by a bridged‐indenyl ancillary ligand, [C₉H₆SiMe₂‐ (CH₂)₂SiMe₂C₉H₆]Ln(µ‐Cl)₂Li(TMEDA) [Ln=Y ( 1 ), Lu ( 2 )], were synthesized via salt metathesis reaction. Reaction of C₉H₇SiMe₂(CH₂)₂SiMe₂C₉H₇ with 2 equiv. of n‐butyllithium in hexane at room temperature afforded [C₉H₆SiMe₂‐ (CH₂)₂SiMe₂C₉H₆]Li₂ as white powder in 95% isolated yield. Further treatment of [C₉H₆SiMe₂(CH₂)₂SiMe₂‐ C₉H₆]Li₂ with anhydrous LnCl₃ in 1:1 molar ratio in THF/TMEDA at room temperature provided the bridged‐indenyl rare earth metal chlorides 1 and 2 in 86%–89% isolated yields. Both complexes were characterized by FT‐IR spectroscopy, NMR spectroscopy, elemental analysis, and X‐ray single crystal structure analysis. The central metals in both complexes are eight‐coordinated by two indenyl ligands in η⁵‐fashion, and two chlorine atoms to adopt a distorted tetrahedral geometry.     

Low-temperature activation of methane over rare earth metals promoted Zn/HZSM-5 zeolite catalysts in the presence of ethylene

At low temperature of 723 K, methane can be easily activated in the presence of ethylene in the feed, and converted to higher hydrocarbons (C2–C4) and aromatics (C6–C10), through its reaction over rare metals modified Zn/HZSM-5 zeolite catalysts without undesirable carbon oxides formation. Methane can get 37.3% conversion over the above catalysts under low temperature, and the catalysts show a longer lifetime than usual metal supported HZSM-5 zeolite catalysts without adding any rare earth metals. The effects of methane activation over various rare earth metal promoted Zn/HZSM-5 catalysts on the products and influences of several reaction conditions such as temperature, catalyst lifetime and molar ratio of CH4/C2H4 have been discussed.     

Optimization of preparative chromatographic separation of multiple rare earth elements

This work presents a method to optimize multi-product chromatographic systems with multiple objective functions. The system studied is a neodymium, samarium, europium, gadolinium mixture separated in an ion exchange chromatography step. A homogeneous Langmuir Mobile Phase Modified model is calibrated to fit the experiments, and then used to perform the optimization task. For the optimization a multi-objective Differential Evolution algorithm was used, with weighting based on relative value of the components to find optimal operation points along the Pareto front. The objectives of the Pareto front are weighted productivity and weighted yield with purity as an equality constraint. A prioritizing scheme based on relative values is applied for determining the pooling order. A simple rule of thumb for pooling strategy selection is presented. The multi-objective optimization gives a Pareto front which shows the rule of thumb, as a gap in one of the objective functions.