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首页> 外文期刊>Journal of Fluids Engineering >Freon Bubble Rise Measurements in a Vertical Rectangular Duct
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Freon Bubble Rise Measurements in a Vertical Rectangular Duct

机译:垂直矩形管道中的氟利昂气泡上升测量

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摘要

A photographic technique was used to obtain the terminal velocity and shape of isolated Freon-114 bubbles in a 3.3 X 15.24 cm rectangular test section. A 120 mm still camera equipped with a high magnification lens faced the test section, while a 200 W strobe lamp flashing at 200 Hz illuminated the bubbles from the opposite side. This technique allowed the bubble diameter and velocity to be obtained from a single photograph. The bubble rise data were taken over a bubble Reynolds number range of 52-1300 for zero liquid flow. At Reynolds numbers less than 118, the bubble shape was spherical. As the Reynolds number increased, the pressure difference between the front and side surfaces of the bubble increased. This caused the aspect ratio (defined as the ratio of bubble height to width) to drop until a relatively constant value of 0.35 was obtained. The drag coefficient was calculated from the measured values of bubble size and velocity using an expression derived from a force balance on a single rising bubble. This analysis indicates that the drag coefficient varies between 0.12 and 1.69 for the given Reynolds numbers range. Comparisons of bubble velocity and shape data to available correlations show that Freon bubbles behave similarly to bubbles rising in pure liquid. The rise velocity data exhibits a peak of 21.4 cm/s for bubble diameters near 0.42 mm; this peaking is a general characteristic of pure substances.
机译:在3.3 X 15.24 cm矩形测试区域中,使用照相技术获得了分离的氟利昂114气泡的终极速度和形状。装有高倍率镜头的120毫米静态照相机面向测试部分,而200 W频闪灯以200 Hz的频率闪烁,从相反的一侧照亮气泡。该技术允许从单张照片获得气泡直径和速度。对于零液体流量,在52-1300的雷诺数范围内获取气泡上升数据。雷诺数小于118时,气泡形状为球形。随着雷诺数增加,气泡的前表面和侧面之间的压力差增加。这导致长宽比(定义为气泡高度与宽度的比率)下降,直到获得相对恒定的值0.35。使用从单个上升气泡上的力平衡得出的表达式,根据气泡大小和速度的测量值计算阻力系数。该分析表明,对于给定的雷诺数范围,阻力系数在0.12至1.69之间变化。气泡速度和形状数据与可用相关性的比较表明,氟利昂气泡的行为类似于在纯液体中上升的气泡。上升速度数据显示气泡直径接近0.42 mm时的峰值为21.4 cm / s。这种峰化是纯物质的一般特征。

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