笔式界面软件资源管理模型及其实现*

针对目前文档管理模式和WIMP界面交互范式对笔式交互的不足,提出了笔式界面软件文档资源管理的统一模型,能够有效地管理笔式界面软件所产生的文档数据,并且根据此模型实现了笔式界面的文档资源管理系统,采用了PIBG交互范式和实物界面.评估结果表明,根据此模型设计的系统,能够提高用户工作效率,降低用户的认知负担.     

基于超市模型的网格资源分配方法研究*

针对网格资源管理中的资源分配问题,提出了一种基于超市模型的网格资源管理分配方法.该方法能够实现子资源的快速匹配,从而减少了网格管理开销,更高效地分配了稀缺资源.     

基于连通度的Ad hoc网络路由协议研究与仿真*

对Ad hoc网络各种路由协议进行仿真评估,分析它们在不同约束条件下不同度量的相对性能,是了解与学习路由协议性能的重要手段.目前的度量标准主要集中在吞吐量、延时、抖动、丢包率等QoS因子或路由负载、寻路时间等外部特性上,还没有以Ad hoc网络系统本身的连通度作为度量标准进行仿真,评价各种路由协议在不同试验条件下对于同一网络系统连通度的影响的相关研究.基于能量模型、节点密度、停留时间及移动速率四种约束条件对MANET提出的四种路由协议进行了关于网络连通度的仿真与评估,给出了这方面的初步结论.     

基于块段模型的三维GIS混合数据结构模型研究*

为了有效地表示三维GIS空间实体,在地质块段模型的基础上,提出了基于八叉树和四面体格网的混合数据结构模型(block octree tetrahedron,BOT模型).采用BOT模型生成算法对块段模型进行重新分割,八叉树作整体描述,四面体格网作局部精确描述,并以不同的灰度值表示不同的单元块属性.同时,为节省存储空间,提出了线性BOT编码技术.实验结果表明,BOT模型充分发挥了八叉树和四面体格网的优点,可以在不增加存储空间的前提下实现对三维目标更高效、更精确的表达.     

我国养老保障制度改革面临的问题及对策探讨

在简要回顾我国社会养老保障制度改革历程的基础上,重点剖析了当前我国“混合型”养老保障制度在试运行过程中所存在的问题及其成因,进而有针对性的提出了完善我国“混合型”养老保障制度的建议。     

磁悬浮列车造型仿生设计研究

以仿生设计的理论为基础来指导磁悬浮列车造型设计,以期为列车车型概念提供灵感,提高列车造型品质,并满足车体气动性能的基本要求。首先,通过文献研究归纳了国内外以磁悬浮列车为主的轨道列车造型仿生的研究动向;其次,通过案例研究解析典型仿生设计系列车型案例,探究列车仿生对象的应用形式;再次,综合仿生设计与轨道列车设计的方法要素,构建磁悬浮列车仿生设计的一般程序,并基于车体线性趋势的仿生规律,以平鳍旗鱼为仿生对象,设计具有仿生特征的磁悬浮列车概念性设计造型方案;最后,通过初步的仿真模拟,得到该方案的空气阻力系数。通过将本方案与相关案例数据的对比,证明运用仿生设计可以满足磁悬浮列车造型对美学价值和气动性能的要求。     

数据机房送风孔板处空气流动的数值模拟

以数据中心机房某一孔板及其相邻机柜为研究对象,采用ANSYS有限元分析方法,对孔板和机柜建立3种不同的有限元模型:几何实体模型、缩小送风孔板风口面积的基础模型、将孔板视为多孔介质面并添加源项的优化模型。根据实测数据确定3种模型的边界条件,通过有限元仿真计算获得它们的压力、速度云图,将基础模型和优化模型分别与几何实体模型进行对比。结果表明,优化模型与几何实体模型的速度场和压力场的大小误差在5%以内,同时优化模型的计算时间相较于几何实体模型可以减少60%。     

冠脉造影图像血管增强及减影的优化方法

针对于传统X射线冠状动脉造影序列图像的血管的减影包含严重伪影以及减影结果不完整等问题,提出了冠脉造影图像血管增强以及减影优化的方法。基于冠脉造影序列图像的时空特性,将相同时相的图像匹配进行减影,得到初步减影结果。针对初步减影部分缺失,对有导管遮挡没有被识别的单根血管进行二次增强处理。增强方法为:运用区域生长确定被导管遮挡的血管部分,以此部分为基础按规定模板扩展,形成覆盖导管区域,区分血管和导管,改变两部分的灰度值,增大对比度。最后采用灰度线性变换、中值滤波等步骤,得到优化的冠脉血管减影。实验表明,本减影及优化方法可以从冠脉造影序列图中提取较为完整清晰的冠脉血管并且具有很好的可控性和鲁棒性。     

Developing a talent training model related to chemical process safety based on interdisciplinary education in China

While chemical industrial development in China is growing rapidly, the corresponding safety training resources remain inadequate, which may often lead to increased risk of chemical accidents. These accidents are often associated with the negligence of safety management, poor safety hazard awareness, and lack of safety practice. In order to alleviate these prominent risk factors in chemical industries in China, our study develops a talent training model related to chemical process safety. First, we propose an approach for establishing the “talent training model” related to chemical process safety, consisting of three steps: analyzing the current status and existing problems of talent training related to chemical process safety, determining the theoretical basis and training objectives for developing interdisciplinary talents, and designing a new talent training model. Second, we establish a talent training model using the proposed method, which includes a comprehensive curriculum system, a diversified teaching pattern, and a quintuple evaluation method. Furtherly, we determine the expected outcomes of the talent training model. The research results provide an innovative chemical process safety training method that is applicable nationwide, also it works as a reference for other rapidly developing countries in the chemical process industry to improve safety within the chemical industry.     

Electrolytic cell engineering and device optimization for electrosynthesis of e-biofuels via co-valorisation of bio-feedstocks and captured CO2

Utilizing CO₂ in an electro-chemical process and synthesizing value-added chemicals are amongst the few viable and scalable pathways in carbon capture and utilization technologies.CO₂ electro-reduction is also counted as one of the main options entailing less fossil fuel consumption and as a future electrical energy storage strategy.The current study aims at developing a new electrochemical platform to produce low-carbon e-biofuel through multifunctional electrosynthesis and integrated co-valorisation of biomass feedstocks with captured CO₂.In this approach,CO₂ is reduced at the cathode to produce drop-in fuels(e.g.,methanol)while value-added chemicals(e.g.,selective oxidation of alcohols,aldehydes,carboxylic acids and amines/amides)are produced at the anode.In this work,a numerical model of a continuous-flow design considering various anodic and cathodic reactions was built to determine the most techno-economically feasible configurations from the aspects of energy efficiency,environment impact and economical values.The reactor design was then optimized via parametric analysis.