旋转直线切向流聚丙烯管式膜器环隙切剖面流场测试

实验研究了旋转直线切向流管式膜器环隙切剖面的流场特征.通过建立膜滤实验装置系统,首次采用PIV激光粒子成像测速系统定量实测了旋转直线切向流管式膜器在不同工况,即不同流体压力、不同入口流量或不同人口切向流速等操作参数下环隙切剖面的流线图和涡量图,并在环隙切剖面内测出了流体切向速度和轴向速度及其分布规律:①在非涡区域,无论操作参数如何变化,在横坐标相同时,靠近旋转切向流人口方向的速度比远离人口方向的速度要大;涡内区域流体的速度一般小于涡外部的流体速度;涡心处速度最低,而且切向速度一般为0;涡心附近的切向速度小     

Study on the wind field and pollutant dispersion in street canyons using a stable numerical method

A stable finite element method for the time dependent Navier-Stokes equations was used for studying the wind flow and pollutant dispersion within street canyons. A three-step fractional method was used to solve the velocity field and the pressure field separately from the governing equations. The Streamline Upwind Petrov-Galerkin(SUPG) method was used to get stable numerical results. Numerical oscillation was minimized and satisfactory results can be obtained for flows at high Reynolds numbers. Simulating the flow over a square cylinder within a wide range of Reynolds numbers validates the wind field model. The Strouhal numbers obtained from the numerical simulation had a good agreement with those obtained from experiment. The wind field model developed in the present study is applied to simulate more complex flow phenomena in street canyons with two different building configurations. The results indicated that the flow at rooftop of buildings might not be assumed parallel to the ground as some numerical modelers did. A counter-clockwise rotating vortex may be found in street canyons with an inflow from the left to right. In addition, increasing building height can increase velocity fluctuations in the street canyon under certain circumstances, which facilitate pollutant dispersion. At high Reynolds numbers, the flow regimes in street canyons do not change with inflow velocity.     

A computational model for the rise and dispersion of wind-blown,buoyancy-driven plumes—I. Neutrally stratified atmosphere

A multi-dimensional computational model for the rise and dispersion of a wind-blown, buoyancy-driven plume in a calm, neutrally stratified atmosphere is presented. Lagrangian numerical techniques, based on the extension of the vortex method to variable density flows, are used to solve the governing equations. The plume rise trajectory and the dispersion of its material in the crosswind plane are predicted. It is found that the computed trajectory agrees well with the two-thirds power law of a buoyancy-dominated plume, modified to include the effect of the initial plume size. The effect of small-scale atmospheric turbulence, modeled in terms of eddy viscosity, on the plume trajectory is found to be negligible. For all values of buoyancy Reynolds number, the plume cross-section exhibits a kidney-shaped pattern, as observed in laboratory and field experiments. This pattern is due to the formation of two counter-rotating vortices which develop as baroclinically generated vorticity rolls up on both sides of the plume cross-section. Results show that the plume rise can be described in terms of three distinct stages: a short acceleration stage, a long double-vortex stage, and a breakup stage. The induced velocity field and engulfment are dominated by the two large vortices. The effect of a flat terrain on the plume trajectory and dispersion is found to be very small. The equivalent radii of plumes with different initial cross-sectional aspect ratios increase at almost the same rate. A large aspect-ratio plume rises slower initially and then catches up with smaller aspect-ratio plumes in the breakup stage. The Boussinesq approximation is found to be valid if the ratio of the density perturation to the reference density is less than 0.1.     

Numerical simulation of stratified turbulent two phase flow in aquatic environment

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屋顶形状对街道峡谷内污染物扩散的影响

采用Spalart-Allmaras湍流模型,通过求解二维连续性方程,Navier-Stokes方程及污染物输运方程,模拟了具有不同屋顶形状的街道峡谷的流场及交通污染物浓度场.计算结果与风洞试验结果总体趋势一致.由于屋顶形状的不同,峡谷内的流场会形成顺时针或逆时针方向的旋涡,从而影响建筑物迎风面与背风面污染物浓度分布.在各种屋顶形状的街道峡谷中,壁面污染物浓度的相对大小与其附近的速度分布有直接关系.通过对街道峡谷建筑屋顶高度处垂直方向污染物通量的计算和比较,说明了不同屋顶形状的街道峡谷平均流扩散和湍流扩散的强弱,污染物湍流扩散通量值有可能为正或为负;同时,峡谷内剩余污染物浓度的大小表明了屋顶形状对污染物扩散出街道峡谷难易的影响.      

混凝过程中流场结构的PIV测量与表征

采用粒子成像速度场仪(PIV)在不投加专用示踪粒子的条件下,以混凝絮体为示踪粒子,对Taylor-Couette反应器内的絮凝反应流场进行测量与表征.结果表明,内筒旋转雷诺数Re在900~2900时,流场中产生的涡具有相似的特殊波状涡结构,相邻涡旋形态大小发生周期性变化,涡间存在主流液体的移动,这种涡结构有利于絮体结合生长成较大的絮体颗粒,便于沉降而导致较高的絮凝沉淀去除率.这也证实PIV技术能够在进行混凝反应的同时,用混凝过程中的微絮体为示踪粒子对混凝过程进行流场测量,不必再额外添加示踪粒子,就能较好地反映混凝过程中涡旋的形态变化特征,从而实现对絮凝过程的同步测量与表征.     

地下水原位化学修复数值模拟研究进展

数值模拟是地下水原位化学修复设计的主要方法。从地下水原位化学修复过程的物理和化学作用出发,分析了土体平衡方程、流体相连续性方程和溶质运移方程等基本控制方程,比较了常用地下水原位修复数值模拟软件的特征,指出土体变形对地下水渗流和溶质运移的影响以及现有地下水原位化学修复模拟中存在的问题,需考虑以下3个方面:1)原位注入化学修复模拟时应考虑土体变形、地下水渗流和溶质运移的三维耦合模型和模拟计算;2)药剂注入方式以及药剂注入引起的土体变形和破坏及其对土体渗透性的影响;3)药剂注入对土体固结变形和强度的影响。     

亚微涡旋的混凝作用研究

以粒子图像速度场仪(PIV)测得了Taylor-Couette反应器旋转内筒和固定外筒间的环隙流场图像.所得图像表明环隙间存在亚微尺度的涡旋.同时实验研究了在Taylor-Couette反应器环隙间不同涡旋形态下聚合氯化铝(PAC)对高岭土悬浊液的混凝效能.结果表明,在波涡流(WVF)形态范围内混凝效能达到了最大(50%以上),这可归因于涡的闭合特性及其随时间的膨胀和收缩.但在波涡流形态范围以外得到的混凝效能相对较低,可归因于相互连通的非闭合涡特性.     

横向流中曝气气泡生成动力学及模拟研究

采用水平集方法和变物性的单一流体运动方程,结合显式时间步进的ICE数值算法,三维模拟了推流式曝气池内气泡的生成过程.重点研究了横向水流对曝气气泡生成动力学的影响.模拟的气泡形状演变过程与国外学者的可视化实验符合较好.模拟结果显示,与在静止水流中气泡的生成相比,曝气池内水横向流动对气泡的生成过程有重要的影响.由于受到水流施加的横向曳力作用,气泡逐渐倾斜向下游生长;气泡生成的时间明显缩短;生成气泡的体积也显著地减小.     

油污染全场模拟的湍浮力流动k-ε模型

以通用的k-ε湍流模型为基础,针对油—水两相流动体系的特点,提出了油污染全场模拟的湍浮力流动k-ε模型.模型不仅在控制方程中计及了密度变化,而且在控制方程中加进了浮力项,并对湍流Schmidt数也作了浮力修正.从而计及了浮力对紊动的影响.结果表明,模型的模拟效果非常满意.     

雨滴表面惯性粒子捕集的湍流效应数值分析

雨滴对气溶胶粒子的清除系数与捕集效率密切相关,并依赖于雨滴附近的气流型式.考虑到实际大气背景均为湍流状态,分别对层流和湍流状态下大尺寸雨滴表面上惯性粒子的捕集过程进行了数值模拟,讨论了湍流脉动对不同粒子轨迹的畸变和扰动.结果表明,层流条件下的模拟结果与已有的实验结果具有很好的一致性.若对雨滴的绕流附加一个湍流强度,则雨滴附近流动速度的随机变化将对粒子的运动轨迹产生明显的影响,导致惯性粒子在湍流状态下被雨滴捕获的效率大于层流捕集效率,湍流脉动效应对粒子捕集效率的提高幅度随粒子尺度的增大而减弱.     

Prediction of vortex height from mechanical mixing in metal matrix nanocomposite processing by means of dimensional analysis and scaling

Mechanical mixing can be used for initial dispersion and distribution of nanoparticle agglomerates in metal matrix nanocomposite (MMNC) fabrication. As vortex height increases, flow is enhanced as well as the risk of oxidate melt contamination. The goal of this study was to examine and predict vortex height using dimensional analysis while varying fluid and the angular speed of a pitched square-blade impeller. An equation proposed by Markopoulos et al. was verified for the present experimental conditions. The relevant dimensionless numbers were the Reynolds (Re), Froude (Fr) and Galilei (Ga) numbers. A modified Fr was defined (Fr*) including the shaft and blade angles of the impeller. Experiments allowed calculation of the dimensionless numbers. Two fluids, water and 50 vol% aqueous glycerine, were used. Angular clockwise speed varied from 200 to 900 rpm in 100 rpm increments. Vortex height was measured in lateral view digital images. Correlations of the dimensionless numbers yielded, first, a linear relationship of the product of dimensionless vortex height (H) and specific gravity (ρ*) with respect to Fr*. A polynomial relationship was found between H and ReFr* for each fluid. The polynomial coefficients, in turn, follow a power law behavior with respect to Ga. This allows a prediction of vortex height in other Newtonian fluids that satisfy the single-phase isothermal flow condition. Perhaps, molten aluminum used in MMNC fabrication, can be analyzed based on a simple, room temperature, low cost transparent fluid system. For the experimental conditions in this study, the equation proposed by Markopoulos et al. was valid. The predicting methodology was verified with experimental results using 25 vol% aqueous glycerine, resulting in an absolute percent error of 5.29%, comparable and lower than an error of 9.12% obtained by predicting vortex height with Markopoulos’ equation.     

上游建筑对街道峡谷内流场和污染物分布特征的影响

利用数值模拟方法研究了不同的上游阻挡建筑布局下,行列式和错列式街谷内气流速度和污染物浓度场特征.结果指出,阻挡建筑的存在改变了街谷内的二次流,从而对流场和浓度场均有明显影响.在行列式街谷中,无论上游建筑以何种布局存在,都会减小街谷内污染物浓度.若不考虑上游建筑的存在,将会过高估计行列式街谷内污染程度;在错列式街谷中,与街谷建筑并列的上游阻挡建筑会减小街谷内污染物浓度,而与街谷建筑错列布置的阻挡建筑会增大街谷内污染物浓度;数值模拟结果还表明,街谷内污染物的扩散和清除效果受气流速度和涡流特性的共同作用.     

电除尘器气流分布数值计算方法研究

运用CFD方法对电除尘器内的气流流动进行数值计算,以相应的电除尘器气流分布模型试验为验证算例。数值计算采用多孔介质模型简化进口喇叭气流分布板,以第一电场进口断面的气流速度分布趋势及相对均方根值为评判标准,对比3种不同导流片布置方案的模型实测结果与数值计算结果。结果表明:各方案模拟结果与试验结果均吻合较好,最终布置方案的数值计算结果满足电除尘器设计要求。     

含裂隙介质污染物输运及生物降解不同时间尺度过程的计算方法

讨论了含裂隙介质地下水污染物输运与生物降解非线性方程组数值求解方法。用三次迎风插值方法计算裂隙介质中常见的场变量陡变化问题，用劈裂算子法，解决了方程中对流扩散过程与生化过程非线性耦合，并对快速生化反应项，利用对流项与该反应项的特征时间量级估算，给出了求生化过程作用子步的时间步长估算办法。用上述方法所得到的模拟结果与解析和实验结果对比，吻合很好。     

Direct numerical simulation of the motion of circular pollutant particles in Newtonian fluid

An improved implementation of distributed multiplier/fictitious domain method is presented for the direct numerical simulation of particulate flow. The key improvement is to replace a finite-element triangulation for the velocity and a “twice-coarser“ triangulation for the pressure with a rectangular discretization for the velocity and pressure. For code validation, the sedimentation of a single particle in a twodimensional channel was simulated. The results showed that the simulation is independent of the mesh size as well as the time step. The comparison between experimental data and this simulation showed that our code can give a more accurate simulation on the motion of particlesthan previous DLM code. The code was then applied to simulate the sedimentation of 600 particles in a rectangular box. The falling course ispresented and discussed. At the same time, this simulation also demonstrates that the method presented in this paper can be used for solving the initial problems involving a lager number of particles exaclly with computing durations kept at acceptable levels.     

西南涡对气溶胶光学厚度变化特征的影响研究

为研究西南涡对气溶胶光学厚度(AOD)的影响,本研究利用2008—2010年的西南涡个例数据与对应时间段的中分辨率成像光谱仪(MODIS)卫星遥感观测AOD数据,并结合降水量、风速、相对湿度、温度等气象资料进行了分析研究.结果发现,2008—2010年产生干涡31个,强降水涡29个,弱降水涡26个.总体而言,干涡过境后使AOD增加而降水涡过境后使AOD减少,且弱降水涡比强降水涡削减作用强.春季产生的西南涡对AOD的影响最大,夏季产生的干涡过境后会使AOD减少,夏季的弱降水涡过境后会使AOD增加.不同季节产生的不同类型西南涡过境后致使AOD变化的主导气象因子不同.总体而言,较大的风速对AOD具有显著的削减作用;干涡中较小的风速、温度和相对湿度是使AOD增加的主要因素;弱降水涡中较大的风速和产生的降水是使AOD减少的主要因素,但夏季产生的弱降水涡中影响AOD的主要因素是风速、温度和湿度;强降水涡中无明显的主导因素.     

格子玻尔兹曼方法(LBM)及其在微通道绕流中的应用

介绍了格子玻尔兹曼方法基本理论与计算方法,并建立了D2Q9计算模型,对宏观尺度及微通道中的非稳态绕流进行了数值模拟,得到了绕流过程的速度分布和涡量分布等信息,对流场结构、固体阻力、尾涡脱落等变化规律进行了分析。结果表明,格子玻尔兹曼方法以其计算稳定、效率高等优势能够应用于微反应器领域的数值模拟;同等液相停留时间条件下,微反应器中的圆柱绕流湍动程度明显降低,未形成周期性涡流,流动更加均匀稳定,有助于实现化学反应的精确控制。     

混凝过程中絮体形貌的PIV成像观测与表征

采用粒子成像速度场仪(PIV)对Taylor-Couette反应器内的混凝过程中絮体的微观形貌进行了观测与表征.结果表明,内筒转速在20～60r/min范围内,生成的絮体颗粒较大,粒径分布均匀,絮凝沉淀效果最好.由于内筒旋转速度的变化直接导致混凝流场形态的变化,所以混凝过程中流场形态的变化对絮体生长过程有重要影响,进而直接影响到混凝效果.混凝过程中流场的周期性变化、涡间存在液体传递的波状涡结构有利于絮体颗粒的结合生长,并导致较高的絮凝沉淀去除率.这也说明PIV技术能够在测量流场的同时较好地反映混凝过程中微絮体的形貌变化特征,从而实现对絮凝过程的原位观测与表征.     

车载雷达工作室三维空气流动与传热数值模拟

应用计算流体力学和计算传热学方法对某车载雷达工作室内的三维空气流动和传热进行了模拟与数值计算.建立了车载雷达工作室内三维空气流动与传热计算的物理模型和数学模型,应用κ-ε紊流方程模型、非结构化网格和有限容积法对某车载雷达工作室内的空气流场与温度场进行了三维数值仿真计算与分析,为该车载雷达工作室生存环境的改善与优化提供了...