基于AADL的综合航电分区系统可调度性判定

综合模块化航电(IMA)系统中的分区系统提高了其可靠性和安全性,但在系统设计和实现过程中,应采用各种分析和验证方法确保系统的时间需求得到满足。为此,针对符合ARINC653规范的IMA系统,根据分区系统层级调度的特性,提出一种基于仿真的分区任务集可调度性判定方法。借助Cheddar工具及其自定义调度策略功能,使架构分析和设计语言(AADL)具有对分区系统进行建模的能力,并利用该工具对AADL模型进行仿真以判定系统的可调度性。实例分析结果表明,该方法能自动、准确、快速地进行可调度性判定,并以甘特图的方式绘制任务调度过程,得到直观、详细的结果。     

鼠标的组合型腔浇注系统优化设计

本文将注塑系统平衡的理论和数值模拟技术紧密结合起采，研究鼠标组合型腔的浇注系统。如果熔体不能同时到达各浇口并充满各个型腔，将导致压力分布不均匀，使制品的质量下降，以至于出现充不满等问题，本研究对浇注系统优化，得出了一组最佳的浇注系统方案，从而保证熔体能够基本上在同一时间充满型腔，实现熔体的平衡流动。从分析结果可知，要平衡熔体在组合型腔内的流动，分流道的截面形状和尺寸起到非常大的作用。     

基于多尺寸网格的LEACH协议改进

针对低功耗自适应集簇分层型(LEACH)协议中节点采集的数据存在大量冗余和能量消耗不均衡问题,提出一种能量高效路由协议MDG-LEACH。该协议基于虚拟网格和多尺寸网格选取活跃节点,采用综合考虑节点剩余能量和空间分布情况的簇头选择机制,簇头与基站之间根据动态规划方法建立最短传输路由树进行数据传输。仿真结果表明,与LEACH协议以及单剑锋的LEACH改进协议(计算机技术与发展,2013年第2期)相比,MDGLEACH协议在均衡节点能量消耗和延长无线传感器网络寿命方面有了较大提高。     

原油常减压蒸馏装置的模拟

用石油馏分的蒸馏曲线(ASTM或TBP)和整体密度进行虚拟组分切割，以单元模块组合法严格求解常减压蒸馏塔，建立原油减压蒸馏装置的流程模拟系统。     

一种环境感知的仿真服务调度模型

针对传统分布式仿真框架HLA/RTI中动态调度负载平衡较差、执行可靠性较低的问题,提出一种基于环境感知的仿真服务调度模型C3SM。C3SM模型包含总体结构、调度策略和服务部署。总体结构规定各个模块的功能与交互接口,调度策略采用改进的蚁群算法进行仿真服务的动态调度,服务部署采用重叠覆盖部署策略以保证较好的服务可用性和较低的资源消耗。仿真实验结果表明,与传统分布式仿真框架HLA/RTI相比,C3SM模型通过实时获取执行环境的上下文信息,能够获得较优的负载平衡度,且重叠覆盖的仿真服务部署策略使得仿真运行系统的可靠性明显提高。     

Partitioning of polymers into pores with surface interactions at dilute solution limit

The partitioning of a single polymer chain into a slit in a good solvent with different surface interactions is examined through Monte Carlo simulations from subcritical regime to adsorptive regime. The chain conformation in the subcritical regime is not perturbed by the surface interactions significantly. In the adsorptive regime, the conformation of the chain is strongly perturbed by the surface interactions. The confinement free energy in the two regimes maybe written in a uniform formula, βΔμ_conf∼c₁N(a/D)^xε_w+c₂N(a/D)^1/ν with x∼2.0 or larger in the subcritical regime and ∼1.0 in the adsorptive regime, where ν is the Flory exponent, D is the slit width, N is the chain length, a is the monomer size, and ε_w is the surface interaction energy between the polymer beads and the slit. This formula is valid for a long chain in the narrow slit in the subcritical regime or when the adsorption layer h>D in the adsorptive regime. A critical behavior occurs when ε_w is at the critical adsorption point and x=1/ν, then Δμ_conf will have little dependence on N or D. Higher order terms that are neglected in the above equation, however, may be present that could lead to a weak dependence of K on N and D even in the critical adsorption point.     

Modeling of fast pulse responses in the Multitrack: an advanced TAP reactor

A detailed transport model for the Multitrack setup, a TAP-like system, has been developed, which allows further analysis of adsorption, diffusion and catalysis phenomena. This includes the transport in the void part between the pulse valve and the reactor inlet. The effects of viscous flow and thermal transpiration, aspects that have not been studied in detail before for this type of setup, have been analyzed. A new expression for the modeling of the output signal is proposed depending on the positioning of the MS detector used in the study. The transport parameters of the model have been estimated by the analysis of the experimental pulse responses of the empty reactor system and the reactor charged with an inert packed bed. The proposed model reproduces the experimental pulse responses very well, and therefore can be extended to study systems with reacting or adsorbing beds by including the corresponding rate equations for the processes occurring in the bed of particles.     

流变参数对顺序共注成型芯层熔体最大填充量的影响

基于Hele-Shaw模型，采用有限元数值模拟技术，系统研究了壳层熔体流变指数和零切黏度对顺序共注成型芯层熔体最大填充量的影响规律，并基于流变学理论揭示了其影响机理，最终提出了顺序共注成型芯层熔体最大填充量与壳层熔体流变指数和零切黏度经验关系方程。     

环流式旋风除尘器内流场的数值模拟

采用 CFD 模拟软件 Fluent 6.2 提供的雷诺应力模型(RSM)对环流式旋风除尘器内的流场进行了数值模拟研究.并与热线热膜风速仪实验测试结果进行了比较.模拟结果与实验结果基本吻合.结果表明:环流式旋风除尘器特殊的流路设计,避免了内外旋涡的相互干扰,增强了旋转速度,规整了流形,减小了强湍流对性能的影响,消除了旋风除尘器易产生的短路流和二次返混,提高了除尘效率,降低了设备的压降.通过对影响除尘器性能的局部涡进行分析,为进一步优化结构提供了参考依据.     

高温大颗粒气固流化床流化行为数值模拟

通过数值模拟,对内含直径为3 mm流化颗粒的二维高温流化床开展了研究。其中欧拉途径被用于描述气相运动,而对颗粒相描述则采用拉格朗日途径。采用离散单元法跟踪颗粒在不同时刻位置和速度。结果表明:与300K时相比,1 000 K高温床的临界流化风速有所提高,压降脉动及床层最大膨胀比明显降低。1 000 K时,流化数提高至1.67,高温床内可见到大尺寸的气泡。在气泡之外上、下2个区域中处于气泡对称轴上的颗粒,水平速度具有相反的方向;而y方向上,这二部分颗粒群的速度均向上并大致在10-1m/s范围之内。