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首页> 外文期刊>International Journal of Multiphase Flow >Experimental study on the transition between stratified and non-stratified horizontal oil-water flow
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Experimental study on the transition between stratified and non-stratified horizontal oil-water flow

机译:分层与非分层水平油水流过渡实验研究

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The effect of oil and water velocities, pipe diameter and oil viscosity on the transition from stratified to non-stratified patterns was studied experimentally in horizontal oil-water flow. The investigations were carried out in a horizontal acrylic test section with 25.4 and 19. mm ID with water and two oil viscosities (6.4 and 12. cP) as test fluids. A high-speed video camera was used to study the flow structures and the transition. At certain oil velocity, stratified flow was found to transform into bubbly and dual continuous flows as superficial water velocity increased for both pipe diameters using the 12. cP oil viscosity. The transition to bubbly flow was found to disappear when the 6.4. cP oil viscosity was used in the 25.4. mm pipe. This was due to the low Eotvos number. Transition to dual continuous flow occurred at lower water velocity for oil velocity up 0.21. m/s when 6.4. cP oil was used in the 25.4. mm ID pipe, while for U_(so)> 0.21 m/s, the transition appeared at lower water velocity with the 12. cP oil.The effect of pipe diameter was also found to influence the transition between stratified and non-stratified flows. At certain superficial oil velocity, the water velocity required to form bubbly flow increased as the pipe diameter increased while the water velocity required for drop formation decreased as the pipe diameter increased. The maximum wave amplitude was found to grow exponentially with respect to the mixture velocity. The experimental maximum amplitudes at the transition to non-stratified flow agreed reasonably well with the critical amplitude model. Finally, it was found that none of the available models were able to predict the present experimental data at the transition from stratified to non-stratified flow.
机译:在水平油水流中,实验研究了油水速度,管径和油粘度对分层到非分层模式过渡的影响。研究是在水平丙烯酸测试段中进行的,水平测试段的内径为25.4和19 mm,用水和两种油粘度(6.4和12. cP)作为测试液。高速摄像机用于研究流动结构和过渡。在一定的油速下,使用12 cP油粘度,随着两种管径的表观水速增加,分层流会转变为气泡流和双重连续流。发现到6.4时,气泡流的过渡消失了。 cP油粘度用于25.4。毫米管。这是由于Eotvos号码较低。在较低的水速下,油速高达0.21时,发生了向双重连续流的过渡。 6.4时的m / s。 25.4中使用了cP油。内径为mm的管道,而当U_(so)> 0.21 m / s时,在油压为12 cP的情况下,在较低的水速下会出现过渡。管道直径的影响也影响分层流和非分层流之间的过渡。在一定的表观油速下,形成气泡流所需的水速随管径的增加而增加,而形成液滴所需的水速随管径的增加而降低。发现最大波振幅相对于混合速度呈指数增长。过渡到非分层流时的实验最大振幅与临界振幅模型相当吻合。最后,发现没有可用的模型能够预测从分层流向非分层流过渡时的当前实验数据。

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