Settling velocities of particles in bubbly gas-liquid mixtures

The axial dispersion-sedimentation model is commonly used to describe the axial concentrations of solids in three phase bubble columns at low liquid velocities. When the two parameters of this model, the particle settling velocity and the solids axial dispersion coefficient, are uncoupled by the use of various assumptions, physically unrealistic values of these parameters often result. Direct experimental measurements of solids settling rates in bubbly gas-liquid mixtures were carried out. The measured mean settling velocities decreased slightly with gas flow rate and were equal to or slightly less than the single particle free settling velocity in the liquid alone. Solids axial dispersion coefficients were also obtained from the solids settling rate distribution data, and gave values considerably less than the experimental liquid axial dispersion coefficient.     

用CCD摄像法测量下喷环流反应器内的气泡行为

本文开发了一种集高速视频分析系统和计算机数字图像处理技术于一体的具有普适性的动态高速ＣＣＤ摄像系统，并利用该系统测定了两相三维下喷环流反应气内的环境气泡行为，考察了不同喷咀和操作条件对气泡行为及平均传质比表面积的影响。     

原位气泡拉伸法在高聚物中纳米粒子的分散机理及超声振荡研究

探讨了利用原位气泡拉伸法(ISBS法)分散添加在高聚物中的纳米无机添加物的分散机理。ISBS方法可以用来分散添加在高聚物熔体中的固体颗粒团聚体。结果表明：首先ISBS方法是一种有效的原位双向拉伸分散方法；理论计算表明，当气泡膨胀时，在气泡周围可以产生高达10^6s^-1的拉伸速率场，它比传统的挤出设备所能提供的10^3～10^4s^-1的拉伸速率高两个数量级。     

内构件存在时提升管内流动及颗粒混合行为研究

he hydrodynamics and solids mixing behavior in a riser with blunt internals are studied. A uniform radial distribution for solids fraction and particle velocity achieves near the internals. The turbulent velocity of particles near the wall increases with the addition of the internals, with the lateral solids mixing enhanced significantly. Probability density distribution of particle velocity is bimodal in the riser with internals, which is similar to that in the conventional riser, indicating that no significant difference in the micro flow structure exists between the riser with internals and the conventional riser. At the same time, the axial solids mixing behavior changes insignificantly with the addition of internals. These results indicate that the micro flow structure in the riser is very stable, which changes insignificantly with the change of the bed structure.     

气液两相流中气泡形态及运动特征参数提取

对气泡发生装置中竖直向上气泡的形态及运动特征提取方法进行了研究。采集原始气泡图像,进行图像灰度化、差影和中值滤波等图像预处理,针对气泡图像的特点,提出动态阈值压缩大津法进行阈值分割,并结合扫描线种子填充算法与图像形态学运算进行孔洞填充,同时基于边缘面积属性对气泡特征区域进行自动识别。实验结果表明,该方法简单有效,鲁棒性强,可以很好地将目标气泡从背景中分离出来,有效提取气泡周长、面积、圆形度和质心坐标等形态特征参数,并实现气泡运动速度的测量。     

液体温度对空泡生长和溃灭过程的影响

采用光偏转测试系统研究了不同温度纯净水中激光空泡脉动过程,通过实验获得了激光空泡在靶表面膨胀和收缩全过程,确定了空泡的最大、最小泡半径、脉动周期和泡壁运动速度。实验采用0℃到70℃的纯净水,测量了空泡的泡半径和脉动周期等特征参量变化情况。实验结果表明,液体温度是影响空泡脉动的一个非常重要的因素,随着液体温度的增加空泡的最大泡半径和溃灭周期均呈增加趋势。给出了相应的理论解释。     

基于行为金融理论的非理性投机泡沫模型

为了从投资者非理性的角度揭示资产泡沫的生成机理,为股市泡沫监管提供更有效的工具,本文在基于行为金融理论的价值函数基础上,对噪音投资者模型进行改进,从利空和利多两个方面考查投资者行为因素的影响,从而构造出新的非理性投资泡沫模型,并利用我国股市数据对模型进行实证研究.结果证明,该模型更切合事实的非理性投机泡沫的发展过程.     

Cavitation characteristics of pit structure in ultrasonic field

Bubble collecting, bubble holding and micro-bubble ejecting characteristics of pit structure and the influence of cavitation bubble on the development of erosion pit are investigated by means of high-speed photography experiments. Pits tend to collect and hold wandering cavitation bubbles. The air holding phenomenon of pits can be a destination of the incubation period in the process of cavitation erosion. The holding bubble tends to eject micro-bubbles from the top of holding cavitation bubble, making the pit a source of nuclei. With bubbles being held in pits, the diameters of pits increase rapidly. But in the given experiment condition, there is a specific stable value beyond which the diameter of pits will not increase. This characteristic will be helpful in understanding and predicting the cavitation erosion process. Supported by the National Basic Research Program of China (“973” Program) (Grant No. 2007CB714105) and the National Natural Science Foundation of China (Grant No. 50539060)     

HYDRODYNAMIC STUDIES IN FISCHER-TROPSCH DERIVED WAXES IN A BUBBLE COLUMN

Gas hold-up and Sauter mean bubble diameter measurements were made in a 0.051 m diameter by 3 m long glass bubble column in the system, nitrogen-molten wax, with three different waxes (paraffin wax FT-300, Sasol's Arge wax and Mobil's reactor wax). Paraffin wax has a tendency to foam and gas hold-up is a strong function of gas distributor type, temperature and start-up procedure, whereas the reactor waxes do not foam and are much less affected by these variables, In experiments at 265°C with a 1.85 mm single hole orifice plate distributor the gas hold-ups were nearly the same for all three waxes. However, significant differences in Sauter mean bubble diameters were obtained in experiments with different waxes; FT-300 wax produced the smallest Sauter mean bubble diameters whereas Mobil's reactor wax produced the largest bubbles. Addition of 1-octadecanol and octadecanoic acid (up to 10wt%) to the FT-300 paraffin wax caused an increase in gas hold-up and a delay in the foam break-up in runs at 265°C with the 1.85 mm orifice plate distributor.