射流泵湍流场的数值模拟与实验研究

采用k-ε湍流模型和非等间距加密网格,对射流泵流场进行了数值模拟和分析,并对相应的流场进行了实验研究.结果表明,流场轴向速度剖面在扩散管段具有较好的自相似性,而在喉管段则不然;这种速度剖面变化的转折点与喉管的长度有关;流场的湍动能分别在喷嘴出口与扩散管入口处产生峰值,并且前者远大于后者,可见射流泵流场中,湍流主要发生在喉管入口处,湍动能的不平衡将导致额外的能量损失.本研究结果对工程应用有指导意义.     

基于小波变换的鼓泡塔内气液两相湍流多尺度结构分析

在φ476 mm的鼓泡塔内,以0.1～1 m·s-1的高气速,利用Pavlov管测量塔内不同位置液相轴向速度,通过能谱分析发现,在空间区域上采用该方法测得的速度时间序列可分为含能尺度区和惯性子区,再借助7尺度Daubechie2小波分析的方法实现湍流量化指标如局部间歇性测度、间歇指数、尺度能量、涡旋尺寸等的评估.实验结果表明,高频和低频尺度下LIM峰分布表明湍流相干结构和大涡旋与小涡旋串级结构的存在.各小波尺度能量的比较说明,气速增大,高频和低频尺度的能量均增大,其中,含能尺度区间的能量占总能量的97%以上.不同尺度涡旋尺寸的计算证实了接近于塔内径最大涡旋的存在.进一步分析表明,塔壁处的涡旋尺寸约为塔中心处的2倍,含能尺度区间的涡旋尺寸为0.03～0.35 m,气速对涡旋尺寸的影响可以忽略.湍流量化指标的分析有助于揭示湍流中的隐含结构以及高气速下鼓泡塔内湍流流动规律.     

Dust Distribution Study at the Blast Furnace Top Based on k-Sε-upModel

The dust distribution law acting at the top of a blast fumace(BF)is of great significance for understanding gas flow distribution and mitigating the negative influence of dust particles on the accuracy and service life of detection equipment.The harsh environment inside a BF makes it difficult to describe the dust disthibution.This paper adresses this problem by proposing a dust distribution k-Sε-u_pmodel based on interphase(gas-powder)coupling.The proposed model is coupled with a k-Sεmodel(which describes gas flow movement)and a u_pmodel(which depicts dust movement).First,the kinetic energy equation and turbulent dissipation rate equation in the k-Sεmodel are established based on the modeling theory and single Green-function two scale direct interaction approximation(SGF-TSDIA)theory.Second,a dust particle mnovement u_pmodel is built based on a force analysis of the dust and Newton's laws of motion.Finally,a coupling factor that descibes the interphase interaction is proposed,and the k-Sε-u_pmodel,with clear physical meaning.ligorous mathematical logic,and adequate generality,is dleveloped.Siumulation results and o-site verification show that the k-Sε-u_pmodel not only has high precision,but also reveals the aggregate distribution features of the dust,which are helpful in optimizing the installation position of the detection equipment and imnproving its accuracy and service life.     

Effects of free stream turbulence on a turbulent boundary layer on a flat plate with zero pressure gradient part IV: Calculation of the flow field

The effects of free stream turbulence on a turbulent boundary layer were calculated by using a k-ϵ two-equation model. The calculations were performed with respect to velocity profiles on a flat plate, wall shear stress, turbulence energy, integral length scales of turbulence, and decay of free stream turbulence, and the results were compared with the experimental results. The energy of the free stream turbulence and the dissipation values at the leading edge of the flat plate were used as the initial calculation conditions. These initial values of dissipation were determined from the integral length scales of the free stream turbulence at the leading edge. The calculated wall shear stress increased with the free stream turbulence and integral length scales of turbulence. The velocity profiles and turbulence energy agreed well with the experimental results, and the effects of free stream turbulence on the wall shear stress agreed fairly well with those observed in experiments. © 1997 Scripta Technica. Inc. Heat Trans Jpn Res. 25 (2): 65–75, 1996     

Condensation of organic binary mixtures flowing horizontally in a horizontal tube bundle

Both heat and mass transfer in the gas phase and heat transfer in the liquid phase are examined experimentally for film condensation of organic binary mixtures such as ethanol-water and methanol-water. Experimental results on the average heat flux, vapor-liquid interface temperature and liquid-phase Nusselt number are compared with analytical solutions based on stagnant film theory and heat-transfer relationships for film condensation from a pure vapor. Experimental heat transfer results agree well with the analytical solutions, except that the experimental liquid-phase Nusselt numbers under conditions of low mass fraction of water are considerably higher than predicted by the analytical solutions. This high value of the liquid-phase Nusselt number is considered to be caused by dropwise condensation in the liquid phase. However, its effect on the tube bundle is not so remarkable compared with that in gravity-controlled condensation on a vertical surface. This is considered to be caused by the condensate inundation effect. © 1997 Scripta Technica, Inc. Heat Trans Jpn Res, 25(6): 342–361, 1996     

簇状分布的刚性双层植被明渠紊流特性分析

采用RNG k-ε 紊流模型,对簇状分布的刚性双层植被明渠水流进行了模拟和分析;根据时间及空间的双平均方法对植被明渠水流的流速及紊动参数进行了统计。结果表明:簇状分布的植被明渠水流可以分为植物区、间隙区及主流区,不同区域时均流速的大小和分布各异;双层植被明渠水流中,时均流速垂线分布在近床面、低植物顶部附近及高植物顶部附近均出现拐点,脉动强度和紊动能的最大值出现在高植物顶部附近。     

Numerical Simulation on Gas-Solid Two-Phase Turbulent Flow in FCC Riser Reactors(Ⅱ) Numerical Simulation on the Gas-Solid Two-Phase Turbulent Flow

Numerical simulation on the flow,heat transfer and cracking reactions in commercial fluid catalyticcracking(FCC)riser reactors were carried out employing the developed turbulent gas-solid two-phase flow-reac-tion model for FCC riser reactors given in Part Ⅰ of the present paper.Detailed information about the turbulentflow fields in the riser reactor obtained revealed the basic characteristics of the gas-solid two-phase turbulentflows when heat transfer and catalytic cracking reactions were co-existing in the riser.Results showed that thedistributions of the flow,the turbulence kinetic energy and the catalyst particle concentration are not uniform inthe axial,radial and tangential directions.The most complicated part of the riser reactor is the feed injectingzone.The complicated configuration of the turbulent gas-solid two-phase flows would exert a great influence onthe results of interphase heat transfer and cracking reactions.     

蒸汽发生器传热管湍流激励功率谱密度计算

湍流激励是核蒸汽发生器换热管发生流致振动的重要机理之一,也是微振磨损的重要诱因。为计算换热管的微振磨损速率,需要首先获得湍流激励功率谱密度（PSD）,其此前只能通过试验的方法获取。为利用CFD方法获得换热管上的湍流激励功率谱密度,建立了蒸汽发生器换热管束流场的数值模型,基于LES方法计算得到了管束内部的流场分布,提取了传热管上所受流体力并计算得到了其功率谱密度,计算结果与试验结果吻合良好。结果显示,管束内部传热管所受流体力为具有尖峰特征的宽频信号,其能量集中在一定带宽内。其结果为利用CFD方法计算传热管微振磨损建立了基础。     

新型矿用排水泵入口段口环密封结构优化研究

以某型号矿用排水泵入口段口环密封为研究对象,采用数值仿真方法,研究排水泵迷宫密封内部流动特征,分析迷宫密封结构尺寸与形状对其泄漏量的影响。结果表明:迷宫的间隙尺寸对密封性能的影响最大,间隙宽度和节流齿宽度的变化将导致泄漏量的大幅变化;相比直齿结构迷宫密封,异形齿结构有利于湍流充分发展,从而可以提高密封性能;通过分析复杂迷宫密封的内部流场,得到适用于排水泵的优化的迷宫密封结构。     

氨气/甲烷贫预混旋转湍流火焰稳定性及NO生成

为了研究氨气/甲烷掺混燃气在贫预混旋转湍流状态下的火焰稳定性及NO的排放特性,设计建造了一个可视化的旋转湍流燃烧装置,开展了一系列的实验测量研究。研究表明：随着当量比增大,氨气火焰稳定燃烧的范围有所扩大,但当氨气掺混比大于0.60时火焰出现上下振荡现象,继续增加将导致火焰吹熄;NO的排放水平随当量比增加而提高;但在相同的当量比下,NO的排放随氨气掺混比的增加先升高再下降。此外,分别采用化学反应器网络（CRN）方法和一维层流预混火焰计算方法,对相应的火焰状态进行了数值计算分析,虽然计算结果与实验结果误差较大,但其预测的NO排放特性随氨气掺混比、当量比的变化趋势是一致的,对三者之间误差的来源进行了分析。