中文摘要：

这研究的目的是数字地在水平圆形的试管上调查掉落的电影的流动特征。数字模拟被执行用为有一个和二柱体的 2D 配置流畅。液体方法的卷被用来追踪液体掉落电影和煤气液体的接口的运动。热和转移系数上的流动特征的效果可能是显著的，尽管它在以前的研究被忽视了。最高的试管，底部试管上的一些特殊流动特征， intertube 流动模式和流动特征上的液体 feeder 高度的效果上的速度分发和电影厚度特征被学习了。我们的模拟显示那 1 )试管的上面、更低的部分的速度分布不严格地对称、不一致， 2 )电影厚度取决于流动率和尖分布， 3 )最高的试管的流动特征与底部试管的那些不同， 4 )三位校长和二个中间的转变模式被区分，并且 5 )液体喂高度戏掉落的形成上的一个重要角色电影。数字结果在与由 Nusselt 模型和报导结果的理论价值的一个好协议。

英文摘要：

The objective of this study is to investigate numerically the flow characteristics of falling film on horizontal circular tubes. Numerical simulations are performed using FLUENT for 2D configurations with one and two cylinders. The volume of fluid method is used to track the motion of liquid falling film and the gas-liquid interface. The effect of flow characteristics on heat and transfer coefficient may be remarkable, although it has been neglected in previous studies. The velocity distribution and the film thickness characteristics on the top tube, some special flow characteristics on the bottom tube, intertube flow modes and effect of liquid feeder height on flow characteristics have been studied. Our simulations indicate that 1） the velocity distributions of the upper and lower parts of the tube are not strictly symmetric and non- uniform, 2） the film thickness depends on flow rate and angular distributions, 3） the flow characteristics of the top tube are different from those of the bottom tube, 4） three principal and two intermediate transition modes are distinguished, and 5） the liquid feed height plays an important role on the formation of falling film. The numerical results are in a good agreement with the theoretical values by the Nusselt model and the reported results.