FORCED CONVECTIVE MASS TRANSFER IN ANNULI

Mass transfer in annuli has been critically examined for various flow situations. The overall mass transfer rate depends on the hydrodynamic regions prevailing in the annular channel as well as on its dimensions. Theoretically consistent correlations are proposed and recommended for both developed and developing boundary layers under laminar and turbulent flow conditions.     

基于边缘信息车流量检测方法的研究

针对边缘检测中阈值很难确定导致不能准确提取背景边缘信息的问题,提出一种改进的基于边缘信息车流量检测方法。该方法预先对路况边缘图像作削顶处理获取一个恰当的阈值,从而可以准确地提取背景边缘信息;且在车辆计数过程中,结合固定窗法和浮动窗法二者的优点,设计一种新的浮动窗法进行车辆计数。实验结果表明,该方法在实时性、检测速度、正确率等方面得到很大的改进,能够在不同环境下进行正确有效地车流量检测。     

采用主监视窗扩展技术的增强现实三维注册方法

在增强现实三维注册中,采用重新检测策略时顿卡现象严重。提出一种采用主监视窗扩展技术的增强现实三维注册方法。在检测阶段,引入特征点可信度和主监视窗,并设计主监视窗的分割、扩展和调控策略,大幅提升了计算速度;在跟踪阶段,采用基于图像金字塔的光流算法进行特征点跟踪。实验证明,该方法不仅有效缓解了顿卡现象,也提升了系统整体的实时性。     

聚合物熔体在圆锥口型的挤出胀大方程

在聚合物熔体入口收敛流变中引入纯拉伸流变概念，应用张量理论进行了定量分析，导出了一个描述圆锥口型的挤出胀大方程。研究表明，入口收敛拉伸流变，是取合物熔体产生了强烈的弹性形变，导致了较大的挤出物胀大比。     

活性污泥的连续流发酵产氢实验研究

采用好氧活性污泥为种泥,以连续流搅拌槽式反应器(CSTR)作为发酵生物制氢反应装置,对发酵法生物制氢系统的启动和运行进行了实验研究。反应器有效容积为10L,接种污泥取自哈尔滨啤酒厂有机废水好氧生物处理系统的二沉池。反应器在污泥接种量为6.09 g·L~(-1),进水有机物浓度2000 mg COD·L~(-1),pH 5～7,HRT 8 h和(35±1)℃的条件下启动,运行27 d后达到稳定的乙醇型发酵状态,最高产气速率和产氢速率分别达到10.1 L·d~(-1)和5.8 L·d~(-1)。在进水有机物浓度提高到4000 mg COD·L~(-1),其他控制条件不变的情况下,系统可在3 d内重新达到新的平衡,最高产气速率和产氢速率分别达到20.7 L·d~(-1)和10.8 L·d~(-1),而氢气含量和发酵类型未发生改变。     

低高宽比微通道中的流动沸腾不稳定性

以甲醇为工质，在不同进口温度、质量流速、热通量和倾角下对低高宽比矩形微通道中流动沸腾不稳定性进行了研究。在宽广的参数范围内发现存在3类不稳定性：流量漂移静态不稳定性、压力降型脉动动态不稳定性及压力降和密度波复合不稳定性。由于大长径比 （L/D=159.5）实验段本身及实验段上游可压缩容积的存在，导致在水动力曲线负斜率区压力降型脉动的发生。分析了进口温度、倾角、质量流量、热通量等因素对不稳定性的影响，发现压力降型脉动的发生主要取决于质量流量、热通量及进口温度三者的影响，给出了以热力学平衡质量含气率表示的脉动工况界限范围。     

Transient and steady-state deformations and breakup of dispersed-phase droplets of immiscible polymer blends in steady shear flow

Transient and steady-state deformations and breakup of viscoelastic polystyrene droplets dispersed in viscoelastic high-density polyethylene matrices were observed in a simple steady shear flow between two transparent parallel disks. By separately varying the elasticities of the individual blend components, the matrix shear viscosity, and the viscosity ratio, their effects on the transient deformation, steady-state droplet size, and the breakup sequence were determined. After the startup of a steady shear flow, the viscoelastic droplet initially exhibits oscillations of its length in the flow direction, but eventually stretches preferentially in the vorticity direction. We find that at fixed capillary number, the oscillation amplitude decreases with increasing droplet elasticity, while the oscillation period depends primarily on, and increases with, the viscosity ratio. At steady-state, the droplet length along the vorticity direction increases with increasing capillary number, viscosity ratio, and droplet elasticity. Remarkably, at a viscosity ratio of unity, the droplets remain in a nearly undeformed state as the capillary number is varied between 2 and 8, apparently because under these conditions a tendency for the droplets to widen in the vorticity direction counteracts their tendency to stretch in the flow direction. When a critical capillary number, Ca_c, is exceeded, the droplet finally stretches in the vorticity direction and forms a string which becomes thinner and finally breaks up, provided that the droplet elasticity is sufficiently high. For a fixed matrix shear stress and droplet elasticity, the steady-state deformation along the vorticity direction and the critical capillary number for breakup both increase with increasing viscosity ratio.     

In situ visualization of drop deformation,erosion, and breakup in high viscosity ratio polymeric systems under high shearing stress conditions

In this paper, deformation and breakup under simple shear of single molten polymer drops in a polymer matrix were investigated. Flow visualization was carried out in a Couette‐Flow apparatus under relatively high shear rates and temperatures up to 230°C. Drop/Matrix combinations were composed of polystyrene drops of 0.5–0.6 mm in diameter in polyethylene matrix, and ethylene–propylene copolymer drops of approximately the same size in polypropylene matrix. The deformation and breakup processes were studied under steady state and time‐dependent shearing conditions. Either for steady state or time‐dependant shearing conditions, drop elasticity generated at relatively high shear rates helped the drops to align perpendicular to the flow direction, i.e., parallel to vorticity axis. Also, the most striking non‐Newtonian effects for the high viscosity ratio systems were the surface erosion and the drop splitting mechanisms. The particles eroded off the main droplet surface were very fine, in the range of 10–50 μm, and led to a significant reduction in main drop size before its final breakup. © 2006 Wiley Periodicals, Inc. J Appl Polym Sci 100: 2582–2591, 2006     

应用炉膛压力诊断气流床气化炉的火焰状态

气化炉是煤气化技术中的关键设备 .气化炉内火焰燃烧稳定性下降 ,会出现燃烧噪音增加、气化燃烧效率降低及熄火等现象 ,对安全性和经济性产生严重的影响 .对气流床气化炉内不同气化燃烧状态下的火焰压力信号进行了小波分析 .结果表明 ,压力信号在一定频段内的分布与气化炉内火焰燃烧的状态密切相关 ,发现随着火焰燃烧稳定性加强 ,气化炉内压力信号向高频方向移动 ,以此可以建立气流床气化炉燃烧诊断模型 .     

浸渍增重率和反渗率研究

对浸溃过程中浸渍剂沥青的浸入率和反渗率进行了分析与探讨。提出了理想增重率、理论增重率与实际增重率的概念和计算方法。并比较了实际增重率与操作增重率的差别。同时分析了抽真空的绝对压力与施压的绝对压力对各项增重率和反渗率的影响。