垂直降流冷凝过程中界面相变与流动物理的捕捉

IF 5 2区 工程技术 Q1 ENGINEERING, MECHANICAL
Thanh-Hoang Phan , Cho-Ning Huang , Chirag R. Kharangate
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引用次数: 0

摘要

两相配置可以解决海军动力和能源系统对有效散热解决方案的迫切需求。更好地理解相变流中的热输运过程对于为海军科学家和工程师开发新的两相设计工具至关重要。本文通过数值模拟研究了冷凝流动过程中界面相变和流动动力学。一个增强的相变模型,结合依赖于冷凝膜厚度的传质强度系数,实现了垂直下流冷凝。采用二维均匀两相reynolds - average Navier-Stokes模型,结合剪切应力输运k-ω湍流模型。开发的求解器对不同的质量传递函数和网格分辨率进行了彻底的评估,显示出对冷凝表面温度预测的最小依赖。随后,在质量流量为108.67 ~ 413.0 kg/m2s、表面热通量为3.46 ~ 8.67 W/cm2的4个测试工况下,对模型进行了验证。沿管道的预测表面温度曲线与测量结果非常吻合,在所有情况下的平均绝对误差都低于2.0%。此外,详细分析了界面相变和流动特性,包括温度和速度分布。结果表明,液膜的凝结厚度沿管内逐渐增大,并逐渐变得不稳定。冷凝传质主要发生在薄边界层内的液-气界面。此外,液膜内的温度和速度分布在靠近冷凝面和液-气界面处呈现出很大的梯度,遵循类似的趋势。最后,研究了湍流模拟对热输运的影响,特别是阻尼因子,发现湍流模拟对表面冷凝换热和界面液-气动力学有显著影响。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Capturing interfacial phase change and flow physics during vertical downflow condensation

Capturing interfacial phase change and flow physics during vertical downflow condensation
Two-phase configurations can address the urgent demand for effective heat dissipation solutions in Naval power and energy systems. A better understanding of thermal transport processes in phase-change flows is critical for developing novel two-phase design tools for naval scientists and engineers. This study investigates interfacial phase change and flow dynamics during condensation flow through numerical simulations. An enhanced phase change model, incorporating a mass transfer intensity coefficient dependent on condensation film thickness, is implemented for vertical downflow condensation. A two-dimensional homogeneous two-phase Reynolds-Averaged Navier-Stokes model, coupled with the Shear-Stress Transport k-ω turbulence model, is employed. The developed solver is thoroughly evaluated against varying mass transfer functions and mesh resolutions, demonstrating minimal dependence on condensation surface temperature predictions. Subsequently, four test cases with varying mass flow rates of 108.67 – 413.0 kg/m2s and surface heat fluxes of 3.46 – 8.67 W/cm2 are investigated to validate the model against experimental data. The predicted surface temperature profiles along the tube show excellent agreement with measurements, with mean absolute errors below 2.0 % across all cases. Additionally, detailed interfacial phase change and flow characteristics, including temperature and velocity distributions, are analyzed. The results reveal that the liquid film condensation thickness increases and becomes progressively unstable along the tube. Condensation mass transfer predominantly occurs at the liquid-vapor interface within a thin boundary layer. Furthermore, temperature and velocity profiles within the liquid film exhibit high gradients near the condensation surface and the liquid-vapor interface, following similar trends. Lastly, the influence of turbulence modeling on thermal transport is investigated, particularly the damping factor, and is found to significantly affect surface condensation heat transfer and interfacial liquid-vapor dynamics.
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来源期刊
CiteScore
10.30
自引率
13.50%
发文量
1319
审稿时长
41 days
期刊介绍: International Journal of Heat and Mass Transfer is the vehicle for the exchange of basic ideas in heat and mass transfer between research workers and engineers throughout the world. It focuses on both analytical and experimental research, with an emphasis on contributions which increase the basic understanding of transfer processes and their application to engineering problems. Topics include: -New methods of measuring and/or correlating transport-property data -Energy engineering -Environmental applications of heat and/or mass transfer
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