CVD反应器传输过程的三维数学模型

提出了一个同时表示CVD过程的气体流动、温度分布和物质传输的三维数学模型。应用这个模型预报了在含有SiCl_4的氢气流中沉积出Si的锥台式反应器中的速度场、温度场和浓度场。所得的结果有助于增进对这类反应器中的传输过程的认识,模型亦可用于设计参数的最优化,诸如入口流量,锥台倾角等。     

多孔纤维型重整微反应器的等效电阻网络建模

针对应用于重整制氢微反应器的复杂多孔金属纤维载体（PFS）的流速场高效分析难题,建立载体中随机微通道的等效电阻网络分析模型. 基于复杂随机纤维结构的统计网络模型,将纤维载体中三维联通的随机微通道结构及与之相连的进出口腔简化为规则的网络通道结构.借鉴基尔霍夫定律,建立纤维载体的等效电阻网络模型,并确定求解方法. 纤维载体流速场实例分析的结果表明,基于等效电阻网络模型求解的纤维载体流速场与计算流体力学(CFD)方法的结果之间的皮尔森相关系数约为98%,且求解效率约为CFD方法的2.9×10⁴倍. 研究成果为多孔纤维型重整制氢微反应器的设计制造提供了新的支撑方案.     

考虑剪切变形的轴心受压GFRP圆管临界荷载

为了考虑剪切变形对玻璃纤维增强复合材料（GFRP）构件屈曲荷载的影响,利用Engesser剪切变形理论,推导考虑剪切变形和初弯曲的临界荷载. 应用于GFRP圆管时,考虑材料各向异性特征对剪切系数及强度的影响. 对4根具有不同长细比的GFRP圆管试件进行轴压试验. 结果表明,GFRP圆管在截面强度估算时应综合考虑轴向纤维压缩破坏和环向基体拉伸破坏. 所推导的临界荷载计算式的结果和试验结果吻合良好.     

考虑材料参数的刚粘塑性有限元初始速度场自动生成方法

本文采用一种包含材料硬化指数ｎ和速率敏感性指数ｍ的刚粘塑性有限元模型，阶段硬化处理考虑到等效应力公与应变率有关，依据线粘性材料假设，提出了考虑材料参数ｎ、ｍ影响的刚粘塑性有限元初始速度场自动生成方法，改进了文献［３］方法。数值模拟结果与有关文献的计算和实验结果进行了比较，表明本文方法是有效的。     

工作流技术在ASP公共服务平台中的应用研究*

根据项目特点,建立了适合ASP平台的基于协调理论和反馈机制的扩展活动网络模型,采用XML模式的XPDL规范实现过程定义;然后通过DOM解析XML数据文档和J2EE的技术支持实现了系统的轻量级工作流引擎.详细介绍了系统实现中解决的两个关键问题:事务型操作的处理和并发控制,并提出了基于优先级的锁绑定机制.     

天然气井下节流嘴前后压力温度分布的数值计算

针对天然气井安装井下节流装置以后很难测得节流嘴上游压力的情况,从空气动力学的原理出发,提出根据井口采集的数据,从节流嘴下游向上游计算其喉部和上游的压力温度综合值的数值计算方法。采用临界状态判别的新方法,即依据节流嘴出口处的马赫数的值,对节流嘴附近的流态进行判别,再分别计算节流嘴出口处,节流嘴喉部以及节流嘴上游的各参数。对宝1井进行了实例计算,计算结果表明:节流后压力温度骤降,经过激波面后压力温度急剧升高的变化情况。     

西江流域压咸风险调度及其时空传递规律研究

枯水期珠江河口咸潮情势日益加重,径流不确定加剧了压咸风险,严重威胁沿线的供水安全。本文基于概率密度分布描述径流不确定性,构建了单源风险调度基本框架。以西江流域五座水库为研究对象,量化了预报误差与压咸风险的响应关系;揭示了压咸风险的时空传递规律;将压咸风险划分为3个等级;确定出各级风险越级传递的临界阈值。研究表明：随预报误差的增大,压咸风险提前且持续天数增加、风险率增大;压咸风险呈逐时段累积和从上游向下游、从支流向干流的时空传递规律;当预报误差超过±16%、±21%时,压咸风险从轻险越级至中险、中险越级至重险。研究成果对于西江流域压咸风险的调控和粤港澳大湾区的供水安全具有重要的应用价值。     

变流场情景下基于鱼类游泳特性的上溯通道分析

水电开发对洄游性鱼类的生境造成了影响,预测目标鱼类洄游期的上溯通道可为修建过鱼设施提供依据,从而减缓其负面效应。本文选取虎渡溪航电工程的下游河段作为研究区域,将长薄鳅、白甲鱼、异鳔鳅鮀作为目标鱼类,针对几种目标鱼类的游泳能力对不同流速进行分区后,得出了适用于多种过鱼目标的流速适宜度曲线,然后对研究区域过鱼期的典型流量进行了数值模拟。根据流速适宜度曲线对研究区域的多种过鱼目标进行了流速适宜度评价,并由评价结果预测了满足多目标过鱼要求的上溯通道。结果表明：流速适宜度评价最优区域出现的位置随流量变化而有所不同,低流量运行条件下出现在主流区域,而高流量运行条件下出现在主流区域两侧;上溯的通道面积占总面积的比例也随流量变化而有所不同,低流量运行条件下的占比约为高流量运行条件下的3 ~ 4倍。根据预测通道特征,对鱼道的进口布置及电站运行调度提供了建议。该结果可为相关鱼类的保护工作提供依据。     

Fouling characteristics of 90° elbow in high salinity wastewater from coal chemical industry

Due to the high salt content of coal chemical wastewater, pipeline fouling often occurs during wastewater treatment. Fouling will cause the diameter of the pipe to shrink or even block, which is not conducive to the safe and stable operation of the wastewater treatment process. In this paper, the experimental device was designed by using FLUENT software and the fouling deposition mechanisms at different flow velocities and different positions in a 90 deg bend were studied. The experimental results show that when the flow velocity is between 0.2 m·s~(-1) and 0.3 m·s~(-1), the thickness of fouling layer was positively correlated with the flow velocity; when the flow velocity is equal to 0.4 m·s~(-1), the formation of fouling is the most serious; when the flow velocity is between 0.4 m·s~(-1) and 0.7 m·s~(-1), the thickness of fouling layer was negative correlation with the flow velocity; with the increase of inlet velocity, the time for sediment point to develop into sediment surface is shortened. The fouling layer is easy to fall off because of the large shear force on the wall surface of the inner bend of the 90° elbow, so the density of sediment at this position is high.     

Effect of dispersion states (electrostatic/electrosteric stabilization) on particles arrangement in the yttria-stabilized zirconia sediments

In the present work, particle arrangement and their packing in the sediment layer of zirconia suspension were studied. To evaluate the particle settling, aqueous suspensions of zirconia nanoparticles were prepared in different dispersion states. In one state, Dolapix CE64 was used as a dispersant to provide electrosteric mechanism. In another state, pH of the suspension was adjusted at 4 to provide electrostatic mechanism. The other state was the combination of dispersant and pH adjustment which resulted in the most stable suspension. First of all, the stability of all dispersion states was evaluated by zeta potential, sediment volume (SV) and height, viscosity, and packing density (PD). Then, the sediment layers of all suspensions were characterized. Incorporation of electrostatic mechanism was resulted in a main decrease in viscosity with high surface charges, while electrosteric mechanism caused lower sedimentation of particles. Fall velocities of particles/agglomerates were estimated, and the influences of dispersion states on the particles fall velocities were characterized. The microstructural observation revealed homogeneous packing of particles in the sediment layer of the stable suspension demonstrating the proper dispersion of particles. Dolapix CE64 and pH adjustment resulted in a uniform arrangement of particles without agglomeration and spherical and regular granules with a uniform shape.