含钛高炉渣制备CaTiO3-多孔地质聚合物光降解吸附材料

含钛高炉渣作为固体废弃物,国内存量巨大,且其中的钛组元难以提取,导致含钛高炉渣综合利用一直没有得到有效解决。针对当前含钛高炉渣利用率低、附加值低等问题,基于含钛高炉渣成分特点,通过选择性析晶(CaTiO₃优势析出)、碱激发,制备出CaTiO₃-多孔地质聚合物的复合材料。试验结果表明,析晶温度1 400 ℃、保温1 h能够促进CaTiO₃的优势析出,而剩余氧化物以玻璃相形式存在。制备出的CaTiO₃-多孔地质聚合物材料结合了CaTiO₃高光催化活性与多孔地质聚合物比表面积大的优点,对亚甲基蓝具有优异的吸附效果,最大吸附量可达60.4 mg/g。在投加量为50 mg,2 h吸附、3 h光降解条件下,对亚甲基蓝去除率可达94.5%,在治理有机污染领域有良好的应用前景。     

Ni3Al中B和Mg的非平衡晶界共偏聚

在1023－1373K的初始温度和0.05-268.91K/s的冷速范围内，用Auger剖层分析确定含B和Mg的Ni3Al合金中B和Mg的非平衡晶界共偏聚行为，按照溶质－空位复合体迁移机制所导出的描述非平衡晶界偏聚的扩散速率方程解析表达式，很好地模拟了本实验结果，并确定了Ni3Al-B-Mg合金中B及B－空位复合体，Mg及Mg-空位复合体的扩散系数及复合体激活能。     

有机凝胶-热分解法制备MgO，Al2O3，MgAl2O4微细纤维

以柠檬酸、乳酸及金属盐为原料，采用有机凝胶-热分解法制备了微细氧化镁、 α-氧化铝和尖晶石结构铝酸镁纤维。所得纤维结构致密、晶粒细小，直径可小于1μm，长径比大。通过FTIR，XRD，DSC及SEM对纤维前驱体凝胶的结构、热分解过程及热处理产物的形貌进行了表征。凝胶的可纺性与组成凝胶的羧酸盐分子结构、羧酸和金属离子的摩尔比等因素有关。柠檬酸和乳酸中的羧基分别以单齿配位于Mg^2＋和Al^3＋可能形成线性分子[（C6H6O7）2Mg3]，[（C3H5O3）3Al]和[（C6H6O7）4MgAl2]，由这些线性分子组成的凝胶显示出了良好的可纺性。     

矩形花键齿形成形研究

运用有限元数值模拟的方法，针对长轴类矩形花键成形时齿形充型不完整的缺陷进行研究，探讨凹模模面的具体参数和毛坯前端倒角对其产生的影响，最终找到最佳的组合。成功地解决了齿形角隅充不满的难题。为现实生产提供理论依据，模拟结果能够很好地指导生产实践。     

用于气体保护焊的自动混气设备

介绍了一种用于焊接现场的气体保护焊的自动混气设备，该设备能精确控制气体混合比例。设备主要由气体传输、气体混合、信号检测和电气控制几大部分组成。计算机适时采集、显示混合气体的混合比例、输出压力、气体湿度等信息，超限发出声光报警。混气设备通过气体分析仪、比例阀和计算机形成闭环控制，从而实现气体混合比例的精确控制。     

少量Ag对低Cu／Mg比的Al—Mg—Cu—Li合金组织与性能的影响

通过显微硬度测试、拉伸试验、能谱分析、SEM及TEM观察，研究了少量Ag对低Cu／Mg比的Al-Mg-Cu-Li合金微观组织与性能的影响。实验结果表明：Ag的添加提高了该合金的硬度和强度，同时改善了其塑性，并延缓了过时效的发生。微观组织观察表明：Ag的添加促进Z相的均匀弥散析出，同时抑制了S＇相在缺陷处非均匀析出；并且Ag的添加还促使了时效初期合金中δ’相的细化和弥散分布，延缓了δ’相的长大。同时分析了析出相种类对合金塑性的影响。     

Mercury transformation across particulate control devices in six power plants of China: The co-effect of chlorine and ash composition

This paper presents the results of field measurements on mercury speciation in six power plants of China by applying the Ontario hydro method. During the tests, flue gas was sampled simultaneously before and after particulate control devices (electrostatic precipitator and fabric filter baghouse) along with the pulverized coal, bottom ash and fly ash sampling. The amount of oxidized mercury in gas phase before and after ESP/FF suggests that mercury oxidation after combustion is a kinetically controlled process. The comparison of mercury speciation in different power plant indicates a clear relationship with coal type, especially the chlorine concentration and the basic ash compositions in coal. Both of the factors are analyzed quantitatively in this study. A new parameter C (ratio of chlorine in coal to base/acid ratio) has been introduced to evaluate the co-effect of the two factors above on mercury speciation.     

Synthesis and Characterization of 2-(Dimethylamino)ethyl Methacrylate Homopolymers via aqueous RAFT Polymerization and Their Application in Miniemulsion Polymerization

Summary Homopolymers of 2-(dimethylamino)ethyl methacrylate (DMAEMA) have been synthesized directly in aqueous media by reversible addition-fragmentation chain transfer polymerization (RAFT) using 4,4-azobis(4-cyanopentanoic acid) (V501) as a water-soluble azo initiator and 4-cyanopentanoic acid dithiobenzoate (CPADB) as a chain transfer agent. The resulting polymers were controlled in the range of narrow molecular weight distributions, with lower than 1.3. Using the produced dithioester-capped DMAEMA homopolymer as a macro chain transfer agent, miniemulsion RAFT polymerization of methyl methacrylate and styrene were carried out, respectively. ¹H NMR analysis showed that the diblock copolymer PDMAEMA-b-PMMA in the form of stable latices was obtained as expected. This revised version was published online at the end of November 2004. Unfortunately, the received date was incorrect due to a technical problem.     

Modeling circulating fluidized bed biomass gasifiers. Results from a pseudo-rigorous 1-dimensional model for stationary state

Results from a 1-dimensional and semirigorous model for atmospheric and circulating fluidized bed biomass gasifiers (CFBBGs), presented in the (previous) paper by Corella and Sanz [J. Corella, A. Sanz, Modeling circulating fluidized bed biomass gasifiers. A pseudo-rigorous model for stationary state. Fuel Process. Technol. 86 (2005) 1021–1053], are shown here. Process variables predicted by the model are gas composition (H₂, CO, CO₂, CH₄, C₂H_n, H₂O and O₂ contents), gas yield, tar content in the flue gas and char concentration in the solids. Both axial profiles in the riser and values at the gasifier exit are calculated from the model and are shown here for some selected sets of process variables. Variables analyzed in depth are: total air flow (used as equivalence ratio, ER), percentage of secondary air flow, height (location) of the secondary air flow, biomass moisture and biomass flow rate, expressed as the biomass weight hourly space velocity in the gasifier. All the results from the model agree both with known published data and with some tests made to check the model.     

Depth profiles of the Fermi level at an amorphous-carbon nitride/SiO2/n-type-Si heterojunction interface obtained by Kelvin probe force microscopy

To explore the work function of a typical amorphous-CN film containing a nitrogen concentration of 23.5 at.%, surface potential images were acquired using Kelvin probe force microscopy. Based on the Fermi level of the n-type Si and the contact potential difference between the amorphous-CN film and the n-Si substrate, the work function of the amorphous-CN film was estimated to be 5.2 ± 0.2 eV below its vacuum level. Using the surface potential depth profile for an etched amorphous-CN film, energy diagrams of the amorphous-CN/SiO₂/n-Si interface were constructed based on the positional relationship of the Fermi level. These band diagrams showed that band bending occurred at the amorphous-CN/SiO₂/n-Si interface despite the Fermi level pinning effect of surface trapping due to the SiO₂ insulator layer.