共查询到19条相似文献,搜索用时 171 毫秒
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板状燃料组件结构紧凑、冷却剂通道狭窄,其边界层流场特性是决定矩形通道与常规通道内单相流动和传热特性存在差异的重要因素。本文采用粒子图像测速(PIV)技术,对间隙为2 mm和3 mm的矩形通道的速度边界层进行了可视化实验研究,分析了矩形通道边界层内速度分布、雷诺切应力等流场特性,探究了通道间隙对边界层的影响规律。实验结果表明,矩形通道的湍流边界层无量纲速度分布符合Spalding公式,在距离窄边壁面0.2~0.3 mm范围内存在雷诺切应力峰值区,随着雷诺数的增加,速度边界层的黏性底层逐渐减薄,对数律层占比增大,雷诺切应力峰值区向壁面方向靠近。减小矩形通道间隙,将会限制近壁面速度剖面的发展,使得近壁面速度梯度增大,湍流强度减小。 相似文献
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纵向涡对窄间隙矩形通道内流动边界层作用特性研究 总被引:1,自引:0,他引:1
利用纵向涡发生器(LVG)产生纵向涡(LV)强化传热的机理主要是基于对边界层的削薄和破坏。由于LV作用距离远,结构简单,安装高度低,对于具有窄间隙通道的换热结构,LV强化传热有着较强的应用价值。本文应用相位多普勒粒径分析仪对LV作用下的窄间隙矩形通道内速度场分布进行了测量。实验结果表明,LV可以有效地削薄和破坏流动边界层厚度;LV对边界层的削薄和破坏可以对传热起到强化的作用;CFD数值模拟结果表明,剪切应力模型(SST)以对LV作用下窄间隙矩形通道内的速度场进行有效地模拟。 相似文献
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纵向涡发生器作用下矩形通道内流动换热性能研究 总被引:1,自引:0,他引:1
对渐缩式纵向涡发生器与椭圆支柱共同作用下矩形通道内的流动换热性能进行了研究,与渐缩式纵向涡发生器、渐扩式纵向涡发生器和光通道的流动换热性能进行了对比,并利用场协同原理对其换热机理进行了分析。结果表明:纵向涡发生器可增强换热,有利于降低加热板的表面温度,从而提高反应堆堆芯的CHF值。采用JF因子对各矩形通道的综合流动换热性能进行了比较,结果表明,渐缩式纵向涡发生器与椭圆支柱组合结构能以较小的阻力代价得到较大的换热效果,是一种理想的强化换热方式。 相似文献
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《等离子体科学和技术》2016,18(3):331-336
Active boundary layer flow control and boundary layer manipulation in the channel flow that was based on low temperature plasma were studied by means of a lattice Boltzmann method.Two plasma actuators were placed in a row to obtain the influence rule of their separation distance on the velocity profile at three locations and maximum velocity in the flow field.Two plasma actuators were placed symmetrically inside a channel to examine the effect of channel height and voltage on the velocity profile and flow rate.It was found that the channel height controls the distribution of flow velocity,which affected the flow rate and its direction.Increasing plasma voltage had a negative effect on the flow rate due to the generation of a larger and stronger flow vortex. 相似文献
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在可视化观察的基础上,实验研究了矩形通道高宽比对两相流动阻力和流型关系的影响。实验选择了3种通道尺寸的实验段,截面宽度相同,全部为43 mm,高度分别为1.41、3和10 mm,根据受限因子Co,前两个实验段属于窄通道,第3个属于常规通道。实验结果表明:高宽比不同时,随着气相流速的增加,通道内两相流动压降呈不同的变化趋势。对于10 mm通道,低气相流量时重位压降占主要成分,而对于1.41 mm和3 mm通道,摩擦压降占主要成分;随着气相流量的增大,总压降中摩擦压降的比例也增大;对于10 mm矩形通道,可利用压降变化规律确定搅混流的发生范围。 相似文献
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《Journal of Nuclear Science and Technology》2013,50(12):915-923
The authors have been developing a measurement system for bubbly flow in order to clarify its multi-dimensional flow characteristics and to offer a data base to validate numerical codes for multi-dimensional two-phase flow. In this paper, the measurement system combining an ultrasonic velocity profile monitor with a video data processing unit is proposed, which can measure simultaneously velocity profiles in both gas and liquid phases, a void fraction profile for bubbly flow in a channel, and an average bubble diameter and void fraction. Furthermore, the proposed measurement system is applied to measure flow characteristics of a bubbly countercurrent flow in a vertical rectangular channel to verify its capability. 相似文献
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本文以空气和水为工质,对竖直向上矩形通道(40 mm ×1.41 mm ,40 mm ×10 mm )和圆形通道(D=25 mm )内的两相流流型特性进行了可视化研究。气液两相的表观速度分别为:0.03~24.71 m /s和0.03~3.73 m /s。3个实验段内均出现了泡状流、弹状流、搅混流和环状流4种流型,40 mm ×10 mm 和圆形通道中流型特征较为接近,与40 mm ×1.41 mm 通道中流型相比存在明显差别。此外,绘制出了3种通道详细的流型图。对比结果显示,矩形通道窄边宽度对流型转变有显著的影响,随着矩形通道窄边宽度的增加,其流型转变边界更加趋近于圆形通道。 相似文献
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《Journal of Nuclear Science and Technology》2013,50(8):783-791
The authors have developed a measurement system which is composed of an ultrasonic velocity profile monitor and a video data processing unit in order to clarify its multi-dimensional flow characteristics in bubbly flows and to offer a data base to validate numerical codes for multi-dimensional two-phase flow. In this paper, the measurement system was applied for bubbly countercurrent flows in a vertical rectangular channel. At first, both bubble and water velocity profiles and void fraction profiles in the channel were investigated statistically. Next, turbulence intensity in a continuous liquid phase was defined as a standard deviation of velocity fluctuation, and the two-phase multiplier profile of turbulence intensity in the channel was clarified as a ratio of the standard deviation of flow fluctuation in a bubbly countercurrent flow to that in a water single phase flow. Finally, the distribution parameter and drift velocity used in the drift flux model for bubbly countercurrent flows were calculated from the obtained velocity profiles of both phases and void fraction profile, and were compared with the correlation proposed for bubbly countercurrent flows. 相似文献
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板状燃料元件中的矩形窄缝通道具有宽高比大的几何特征,高度方向速度梯度大、分布陡峭,发生过冷沸腾时,近壁面汽泡运动行为将受其影响而改变,其中汽泡滑移现象对沸腾换热影响较大。本文针对矩形窄缝通道中的汽泡滑移行为,构建了包含滑移热流的壁面热流分配模型,并建立机理性的汽泡受力模型和滑移模型计算汽泡脱离直径、浮升直径和滑移距离等辅助参数,开发了一套适用于矩形窄缝通道内向上流动沸腾的壁面沸腾模型。选用Nuthel窄缝通道沸腾实验进行数值模拟验证,结果表明:本文模型可以较好地预测1~4 MPa中低压工况窄缝通道向上流动沸腾的壁面过热度,最大误差相比RPI模型由80%降低至17%;蒸发热流份额和近壁面空泡份额相比RPI模型更低。 相似文献