热毛细对流速度场测试研究

为了探索微重力状态下表面张力驱动流速度场的测试技术，本文在地面进行了模拟实验，对位于热壁下流体中气泡周围的表面张力驱动流进行了研究，并用ＰＩＶ技术测量了流场的速度分布．     

快速镍刷镀层在含磨粒的油润滑条件下的摩擦磨损性能研究

作者在含磨粒的油润滑条件下对快速镍刷镀层的摩擦磨损性能与45~#钢(淬火+低温回火)的进行了对比试验研究。结果表明,镍刷镀层不仅磨损量和摩擦系数始终都比45~#钢的小,而且它的稳定磨损阶段也长而未出现45~#钢那样明显加剧的磨损。作者指出,这主要是由于镍刷渡层组织所含微孔既可吸附和储存润滑油而起辅助润滑作用,又能使磨粒镶嵌于其中而减少磨粒磨损的缘故,而且随着摩擦温升其塑性也得到改善,因而快速镍刷镀层的摩擦磨损性能都比质地致密且硬度更高的45~#钢的好。     

VERIFICATION OF SMOM AND QMOM POPULATION BALANCE MODELING IN CFD CODE USING ANALYTICAL SOLUTIONS FOR BATCH PARTICULATE PROCESSES

For many processes of industrial significance, due to the strong coupling between particle interactions and fluid dynamics, the population balance must be solved as part of a computational fluid dynamics （CFD） simulation. In this work, a CFD based population balance model is tested using a batch crystallization reactor. In this CFD model, the population balance is solved by the standard method of moments （SMOM） and the quadrature method of moments （QMOM）. The results of these simulations are compared to analytical solutions for the population balance in a batch tank where 1） nucleation, 2） growth, 3） aggregation, and 4） breakage are taking place separately. The results of these comparisons show that the first 6 moments of the population balance are accurately predicted for nucleation, growth, aggregation and breakage at all times.     

颗粒在大涡结构中的弥散

气相采用大涡模拟方法,颗粒相采用轨道模型研究了三维后台阶气粒两相湍流流动的大尺度涡结构的瞬时演变过程以及颗粒的瞬时弥散规律.比较了不同入流速度的颗粒在大涡结构中的瞬时弥散特性,尤其研究了高速释放大颗粒的弥散特性.三维流动中大尺度涡结构具有明显的脱离、发展、合并和破碎过程.小颗粒的分布受大涡结构的控制,其空间的弥散过程与流体 大涡结构的空间发展相一致,但是由于三维流动中大涡边缘和中心区的压力差,颗粒在大尺度 涡的边缘出现密集.而大颗粒在流场中的分布受其惯性控制,对气相的涡结构不敏感.高速释放到流场中的大颗粒受惯性影响最大,保持在其原有动量方向上运动.     

Characterization of particle-laden, confined swirling flows by phase-doppler anemometry and numerical calculation

The particle dispersion characteristics in a confined swirling flow with a swirl number of approx. 0.5 were studied in detail by performing measurements using phase-Doppler anemometry (PDA) and numerical predictions. A mixture of gas and particles was injected without swirl into the test section, while the swirling airstream was provided through a co-flowing annular inlet. Two cases with different primary jet exit velocities were considered. For these flow conditions, a closed central recirculation bubble was established just downstream of the inlet.

The PDA measurements allowed the correlation between particle size and velocity to be obtained and also the spatial change in the particle size distribution throughout the flow field. For these results, the behaviour of different size classes in the entire particle size spectrum, ranging from about 15 to 80 μm, could be studied, and the response of the particles to the mean flow and the gas turbulence could be characterized. Due to the response characteristics of particles with different diameters to the mean flow and the flow turbulence, a considerable separation of the particles was observed which resulted in a streamwise increase in the particle mean number diameter in the core region of the central recirculation bubble. For the lower particle inlet velocity (i.e. low primary jet exit velocity), this effect is more pronounced, since here the particles have more time to respond to the flow reversal and the swirl velocity component. This also gave a higher mass of recirculating particle material.

The numerical predictions of the gas flow were performed by solving the time-averaged Navier-Stokes equations in connection with the well known kε turbulence model. Although this turbulence model is based on the assumption of isotropic turbulence, the agreement of the calculated mean velocity profiles compared to the measured gas velocities is very good. The gas-phase turbulent kinetic energy, however, is considerably underpredicted in the initial mixing region. The particle dispersion characteristics were calculated by using the Lagrangian approach, where the influence of the particulate phase on the gas flow could be neglected, since only very low mass loadings were considered. The calculated results for the particle mean velocity and the mass flux are also in good agreement with the experiments. Furthermore, the change in the particle mean diameter throughout the flow field was predicted approximately, which shows that the applied simple stochastic dispersion model also gives good results for such very complex flows. The variation of the gas and particle velocity in the primary inlet had a considerable impact on the particle dispersion behaviour in the swirling flow and the particle residence time in the central recirculation bubble, which could be determined from the numerical calculations. For the lower particle inlet velocity, the maximum particle size-dependence residence time within the recirculation region was considerably shifted towards larger particles.     

两相流中圆柱状粒子阻力的研究

将圆柱状粒子和圆球粒子建立等效关系，由等效面积法得到了作用在圆柱状粒子上的阻力，然后通过有限体积法对圆柱状粒子的阻力进行了数值求解，经比较发现，在层流状态时由等效面积法得到的圆柱状粒子的阻力要乘上一个1．5—2的常系数．     

原位TiC颗粒增强灰铸铁复合材料的组织及其摩擦磨损性能

采用原位反应铸造法制备了TiC颗粒增强灰铸铁复合材料,并考察了复合材料的组织、力学性能和摩擦磨损性能．结果表明：随着合金熔体中Ti含量增加,复合材料中TiC颗粒的数量增加,尺寸减小,而石墨的数量降低,且其形态由片状转化为点状;含有大量TiC颗粒及少量点状石墨的复合材料的力学性能和耐磨性优良,即使在较高载荷下,复合材料中的TiC颗粒和点状石墨仍具有协同减摩抗磨作用,从而使得复合材料的摩擦磨损性能优于普通灰铸铁．     

基于新型滤波器-HABF的SINS传递对准仿真

传统动基座传递对准主要采用扩展卡尔曼滤波技术。但在动基座传递对准的非线性、非高斯条件下,这种基于模型线性化和高斯假设的滤波方法在估计系统状态及其方差时误差较大且可能发散。混合退火粒子滤波针对非线性、非高斯系统状态的在线估计问题,提出一种新的基于序贯重要性抽样的粒子滤波算法。在滤波算法中,用状态参数分解和退火系数来产生重要性概率密度函数,此概率密度函数综合考虑了转移先验、似然、噪声的统计特性以及最新的观察数据,因此更接近于系统状态的后验概率。实验仿真结果表明,这种基于混合退火粒子滤波器不仅比扩展卡尔曼滤波提高了传递对准的精度,而且又比传统的粒子算法减少了时间。     

SiCp尺寸对SiCp／Cu基复合材料抗磨性能的影响

以纳米级(30nm)、亚微米级(130nm)、微米级(14μm)3种粒径的SiCp和微米级(10μm)铜粉为原料，用冷压烧结和热挤压方法制备了纳米、亚微米和微米级SiCp／Cu复合材料，考察了SiCp尺寸对SiCp／Cu复合材料抗磨性能的影响．结果表明，不同尺寸的SiCp颗粒作为增强相均能显著改善铜基复合材料的抗磨性能；随着SiCp尺寸的增大，SiCp／Cu复合材料的抗磨性能提高幅度显著增大，但偶件磨损表面的犁削加剧；以微米级SiCp为原料制备的SiCp／Cu复合材料的抗磨性能最佳，但其导致偶件40Cr钢犁削作用显著加剧．从摩擦副整体的摩擦磨损性能角度而言，宜采用SiCp尺寸为130nm的SiCp／Cu复合材料同40Cr钢组成摩擦副．     

Particle dispersion in a single-sided backward-facing step flow

The paper describes the particle dispersion in a single-sided backward-facing step flow. Particles of well-known sizes in the diameter range from 1 to 70 μm were suspended in an air flow and the particle motion over a step was measured by mean of a laser-Doppler anemometer. Thus, the local and integral flow quantities, i.e. the mean and turbulent velocity data could be measured precisely. In the experiments, monodispersed particle size distributions were used to exclude particle size related information ambiguity, known as triggering effects or size bias. The results of this study show qualitatively and quantitatively the difference in time-averaged particle dynamics for selected particle sizes in a backward-facing step flow. The experiments show, for different sizes, the changes in the particle velocity field in comparison with the velocity field of the continuous phase deduced from the 1 μm particles, and also imply the strong influences which different particle sizes have on flow data evaluation when size effects are not taken into account with particle-related optical measuring techniques.