代理型应用层组播体系结构研究

组通信技术是未来互联网应用的关键支撑技术.目前,应用层组播是组通信技术研究中的热点,而代理型应用层组播体系结构已成为组播体系结构研究的重要方向之一.首先概述和比较了IP组播、主机型应用层组播和代理型应用层组播3种组播体系结构,接着重点研究和分析了代理型应用层组播体系结构的研究现状.以此为基础,进一步总结了代理型应用层组播体系结构设计中需要考虑的基本问题,并针对现有体系结构的不足,探讨了设计新的代理型应用层组播体系结构中值得关注的问题.最后对未来工作进行了展望.     

Fuzzy boundary layer tuning for sliding mode systems as applied to the control of a direct drive robot

Chattering in the control signal is a significant problem in sliding mode control (SMC). The boundary layer approach is one of the many modifications proposed in the literature to avoid the chattering. In this approach, instead of the discontinuous SMC, a continuous feedback control law is employed in a boundary layer around the sliding surface. The thickness of the boundary layer is an important design parameter. This paper proposes a fuzzy online tuning method to adjust the boundary layer thickness for the best system performance without chattering. The method features the measurement of the chattering in the control signal. The paper validates the performance of the algorithm by experiments on a direct drive robot with a range of different payloads.     

网络资源的多层监测方法与实现

设计了针对网络资源不同层次进行监测的实现方法,这些层次包括：网络传输层对象（网络服务器性能、TCP、UDP实现过程）、应用层对象（主要是业务数据库）、表示层对象（页面及相关的脚本行为）、用户（浏览器）以及Web服务（HTTP协议实现过程）。对于不同层次的数据,采用了不同的采集方法,并实现了对不同监测资源的重新组合分析。在分层获取、分析、存储数据基础上进行了统一身份认证、统一展示标准和指标集成展示,从而实现了分布式监测系统的集成。     

催化剂表面上分形杂质对CO氧化反应的影响

担载型金属类催化剂表面,在分子层面上往往有些杂质,也许来自使用中的反应物料.这些结构性杂质会影响催化剂的结构与性能,于是本文引入杂质分形结构的概念,通过Monte Carlo模型去分析和探讨担载型金属催化剂表面CO的催化氧化反应行为.模拟结果发现,催化剂活性中心的不均匀分布,在分形杂质所包围的小区域,O2在催化剂表面活性中心的吸附更加困难.特别是在杂质所占比例较大时,催化剂的活性点在空间被隔离开而形成许多孤立小岛,即使在CO分压较小时,催化剂表面的局部区域也会发生O和CO中毒.随着杂质比例的增加,导致催化剂表面的活性空位分布发生变化,大大减少了CO分子和O原子的接触机会,反应速率随之降低,催化剂活性中心的利用率也降低.     

一种卷板填充分层递归排样的优化算法

研究了卷板填充排样问题,提出了一种分层递归排样的优化算法。算法使用水平剪切线将卷板分层,每层的宽度和卷板宽度相同,高度和层最左端的主毛坯高度相同;通过调用递归过程确定卷板中层的排列,为各层选定主毛坯,并确定毛坯的排列方式;采用分支定界技术缩小搜索空间。实验结果说明该算法比文献中最近报道的几种算法都有效。     

触发器及其在医疗分销管理系统中的应用

触发器是一种特殊类型的存储过程,与数据表紧密相连。它在保持数据库完整性与一致性方面起着非常重要的作用,是一种保证数据库中数据完整性的方法。本文以医疗分销管理系统为例,介绍了触发器的具体应用。     

回转体头部压力分布规律及其对转捩点的影响

以圆头回转体为研究对象,头部线型采用双参数椭圆曲线,利用面元法求解绕流势流流场,利用F.W.Scholkemeier的积分方法,确定该压力分布下的层流边界层,利用P.S.Granville方法求解边界层转捩点.通过变换头部线型参数,以最小压力系数绝对值的下降方向为搜索方向,研究不同头型压力分布的变化规律及其对转捩点的影响.结果表明:最小压力系数绝对值越小的头型其最小压力点离头部驻点的距离越近;不同头型的转捩点不光与其压力分布有关,而且还与其头部长径比有关.     

Microstructure and properties of (Sr, Ca)CuO2/(Sr, Ca)RuO3 multilayers

Epitaxial multilayer thin films of infinite-layer (Sr, Ca)CuO₂ and perovskite (Sr, Ca)RuO₃ have been prepared on (100) SrTiO₃ substrates by multitarget rf magnetron sputtering. X-ray diffraction analyses revealed that the multilayer structure of (Sr, Ca)CuO₃/(Sr, Ca)RuO₃ was successfully fabricated with a minimum layer thickness of 20 Å. Transmission electron microscopy measurements of the multilayers indicated that there was no dislocation which normally exists in single-layer films with an infinite-layer structure. Resistivities of multilayer films at room temperature ranged from 1 to 10 m cm and showed semiconductor-like dependence against the temperature.     

Partial oxidation of isobutene to methacrolein on Bi-W/Fe-Co-Mo-K catalysts

The partial oxidation of isobutene to methacrolein and methacrylic acid was studied on oxidic catalysts containing mainly a mixture of bismuth tungstate and iron-cobalt-potassium molybdate. Catalyst shaping was done by extrusion. The kinetic measurements were performed by monitoring the gas-phase composition along the length of a fixed bed of catalyst. The reactor was treated as an isothermal plug-flow system. The network of parallel and consecutive reactions taking place in this system can be described by a simplified scheme. It is possible to predict the gas-phase composition prevailing in the reactor using five different kinetic parameters. In the temperature range 380<<420°C grain selectivities as high as 85% combined with yields of methacrolein and methacrylic acid about 72% at 92% conversion were obtained.     

Characteristics of Fe/AlPO4-5 catalyst prepared with organic solution

The Fe/AlPO₄-5 catalysts are prepared by impregnation with aqueous and organic solution (acetic acid, alcohol and acetone) of iron(III) nitrite respectively. The characterization of catalyst by means of XPS, Mössbauer spectroscopy, TPR and CO hydrogenation is reported. The catalyst prepared with the aqueous solution has no activity for CO hydrogenation because the Fe(III) in the catalyst cannot be reduced to -Fe. However, the catalysts prepared with organic solution possess obvious hydrogenation activity, in which -Fe is present in the initial reduced catalyst besides Fe³⁺ and Fe²⁺. The results may be explained by the interaction degrees between the metal and the support induced by the different impregnation solvents.