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Numerical Investigation of Laminar Filmwise Condensation of Water Vapor in Horizontal Tube with VOF method in the presence of air

机译:空气存在下vof法在水平管中水蒸气水蒸气的数值研究

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A steady three-dimensional numerical simulation of laminar film condensation of vapor in the presence of air inside a 1 mm horizontal tube is presented. The volume of fluid (VOF) method is used to capture the liquid-vapor interface with a phase change model. According to a generally accepted flow regime map, annular flow pattern is to be expected. Uniform wall temperature and interface temperature are assumed to be boundary condition. The influence of gravity is obvious while the effect of surface tension is neglected. At inlet, the liquid film is thin and evenly distributed around tube wall. Moving downstream the tube, film at the bottom half becomes thicker under the influence of gravity, while film on upper half remains almost constant. Correspondingly, local heat transfer coefficient on bottom half declines gradually and global average heat transfer coefficient shows little difference along axial direction. Existence of air makes heat transfer coefficient decrease sharply compared with that of pure vapor condensation, caused by an existed air layer which increases the thermal resistance during condensation process. As inlet volume fraction of air increases from 0.5% to 3%, the decline trend of heat transfer coefficient slows down.
机译:提出了在1mm水平管内的空气存在下蒸汽的层状膜冷凝的稳定三维数值模拟。流体(VOF)方法的体积用于捕获具有相变模型的液体蒸汽界面。根据通常接受的流动制度图,需要预期环形流动模式。假设均匀的壁温和界面温度是边界条件。重力的影响是显而易见的,而表面张力的效果被忽略。在入口处,液体膜薄型且均匀地分布在管壁周围。下游管道,在重力的影响下,底部的薄膜变厚,而上半部的薄膜几乎保持恒定。相应地,局部的局部传热系数逐渐下降,全局平均传热系数沿轴向表示差异很小。空气的存在使传热系数与纯蒸汽凝结相比急剧下降,其由存在的空气层引起的,其增加了冷凝过程中的热阻。随着入口体积的空气量从0.5%增加至3%,传热系数的下降趋势减慢。

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