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Numerical study of steam condensation inside a long, inclined, smooth tube at different saturation temperatures

机译:不同饱和温度下长而光滑的光滑管内蒸汽凝结的数值研究

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In this study, the effects of the inclination angle on the heat transfer coefficients and on pressure drops were investigated numerically, during the process of development of heat condensation inside a long smooth tube, at different saturation temperatures. The simulation model included a smooth tube with a diameter of 18 mm and a length of 7.2 m. The imposed inclinations varied between -60 degrees (downward flow) to +60 degrees (upward flow). Moreover, the saturation temperatures varied between 40 degrees C and 70 degrees C. The flow field was assumed to be three-dimensional, unsteady, and turbulent. The Volume of Fluid (VOF) multiphase flow method was utilised to solve the governing equations comprising mass, momentum, energy, and turbulence equations, along with phase change rates. The simulation results were in good agreement with the experimental data. The results showed that the condensation heat transfer coefficient first increased and then decreased along the length of the tube. Furthermore, it was noted that the condensation heat transfer coefficient and pressure drop decreased when the steam saturation temperature increased. (C) 2018 Elsevier Ltd. All rights reserved.
机译:在这项研究中,在不同的饱和温度下,在长的光滑管内热凝结发展的过程中,数值研究了倾角对传热系数和压降的影响。仿真模型包括直径为18 mm,长度为7.2 m的光滑管。施加的倾斜度在-60度(向下流动)到+60度(向上流动)之间变化。此外,饱和温度在40摄氏度至70摄氏度之间变化。流场被假定为三维,不稳定和湍流的。流体体积(VOF)多相流方法用于求解控制方程,该方程包括质量,动量,能量和湍流方程以及相变率。仿真结果与实验数据吻合良好。结果表明,冷凝水的传热系数沿管的长度先增大,然后减小。此外,注意到当蒸汽饱和温度升高时,冷凝传热系数和压降降低。 (C)2018 Elsevier Ltd.保留所有权利。

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