A Model for Determining the Rate of Interfacial Heat and Mass Transfer Using the VOF Method for Numerically Solving Evaporation and Condensation Problems

IF 0.9 Q4 ENERGY & FUELS
K. B. Minko, G. G. Yan’kov, T. A. Gataulin, V. I. Artemov, A. P. Zheleznov
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Abstract

The volume-of-fluid (VOF) method, supplemented by models of interfacial heat and mass transfer, is a universal and very effective tool for simulation and detailed analysis of intricate processes occurring in systems with phase transitions. The key feature of this method is that it can quite accurately and in detail describe the physical pattern of running processes in the presence of a sharp phase boundary and provide quantitative data on the distribution of local heat-transfer characteristics and the dynamics of the interphase boundary and associated phenomena, thereby making the VOF method advantageous in researches and engineering practice. Development and improvement of heat and mass transfer models and efficient numerical VOF algorithms, as well as preparation of recommendations for the application of these approaches, are an urgent problem. This paper proposes an approach to the prediction of interfacial heat and mass transfer rate, which is based on the analysis of phase transitions in single-component systems using the linear theory of nonequilibrium processes. The results are presented of verification calculations performed for several standard problems. The classical problems of one-dimensional boiling and condensation (the Stefan problem) are examined as are such problems as vapor condensation in tubes of different orientations, condensation from stagnant or moving vapor on the surface of smooth horizontal tubes, and film boiling on the surface of horizontal cylinders. The predictions are verified against classical solutions and available experimental data. Calculations were carried out for fluids with different thermophysical properties, including water, pentane, propane, R-113, R-21, and R-142b. The maximum ratio of the densities of liquid and vapor phases was as high as 1600 (water at atmospheric pressure). The simulation results demonstrate the versatility of the proposed approach, which allows us to recommend it for solving a variety of engineering problems.

Abstract Image

用VOF法计算蒸发和冷凝问题的界面传热传质速率模型
结合界面传热传质模型的流体体积(VOF)方法是一种通用的、非常有效的工具,可以模拟和详细分析相变系统中发生的复杂过程。该方法的主要特点是能够相当准确、详细地描述存在尖锐相边界的运行过程的物理模式,并提供局部传热特性分布、相间边界动力学及相关现象的定量数据,从而使VOF方法在研究和工程实践中具有优势。发展和改进传热传质模型和有效的数值VOF算法,以及为这些方法的应用准备建议,是一个迫切的问题。本文提出了一种基于非平衡过程线性理论对单组分系统相变分析的界面传热传质速率预测方法。给出了对几个标准问题进行验证计算的结果。研究了一维沸腾和冷凝的经典问题(斯蒂芬问题),以及不同方向管内的蒸汽冷凝,光滑水平管内停滞或运动蒸汽的冷凝以及水平圆柱体表面的膜沸腾等问题。用经典解和现有实验数据验证了预测结果。对不同热物理性质的流体进行了计算,包括水、戊烷、丙烷、R-113、R-21和R-142b。液相和气相密度的最大比值高达1600(大气压下的水)。仿真结果证明了所提出方法的通用性,使我们能够推荐它用于解决各种工程问题。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
CiteScore
1.30
自引率
20.00%
发文量
94
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