Simulation of Film Condensation from Moving Vapor of Refrigerant-21 on a Horizontal Tube Bundle Using the VOF Method

IF 0.9 Q4 ENERGY & FUELS
K. B. Minko, V. I. Artemov, A. A. Klement’ev
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引用次数: 0

Abstract

Considerable progress has been made by now in developing mathematical models, algorithms, and available computational tools for simulating heat and mass transfer processes. Advanced approaches yield detailed information on various characteristics of mass transfer in two-phase fluids, in particular during film condensation of vapors. Models developed by various teams are implemented in CFD-codes (ANSYS Fluent, OpenFOAM, Star-CCM+, etc.). To check existing models and select the best one, cross-verification of models and algorithms implemented in various CFD codes and their verification against available and reliable experimental data are needed. In this paper, cross-verification of the VOF (Volume of Fluid) model and the algorithms implemented in the author’s ANES code was carried out against the problem of vapor condensation on a single tube. The calculations were performed using the ANES and ANSYS Fluent CFD-codes. The predictions by the ANSYS Fluent code have been demonstrated to depend on the settings of the algorithms for solving the conservation equation for the liquid volume fraction. Recommendations are presented for setting this code to obtain better agreement of the predictions with experimental data and theoretical relationships. The ANSYS Fluent code was used for two-dimensional simulation of refrigerant-21 condensation in a small tube bundle. Characteristics of the tube bundle (bank) were equal to those of the tube bundle used in the experimental setup of the Institute of Thermophysics, Siberian Branch, Russian Academy of Sciences (tube diameter = 16 mm, transverse tube bundle pitch \({{S}_{1}}\) = 26 mm, longitudinal tube bundle pitch \({{S}_{2}}\) = 15 mm). Condensation of saturated vapor having a saturation temperature of \({{T}_{{sat}}}\) = 333.15 K and arriving at the tube bundle at a velocity of up to 1.2 m/s was studied. The predictions demonstrate qualitative and quantitative agreement with the experimental data.

Abstract Image

Abstract Image

使用 VOF 方法模拟水平管束上移动的制冷剂-21 蒸汽的薄膜冷凝现象
摘要 目前,在开发用于模拟传热和传质过程的数学模型、算法和可用计算工具方面已经取得了相当大的进展。先进的方法可提供有关两相流体中传质的各种特性的详细信息,特别是在蒸汽的薄膜冷凝过程中。不同团队开发的模型已在 CFD 代码(ANSYS Fluent、OpenFOAM、Star-CCM+ 等)中实施。为了检查现有模型并选择最佳模型,需要对各种 CFD 代码中的模型和算法进行交叉验证,并根据现有的可靠实验数据对其进行验证。本文针对单管上的蒸汽凝结问题,对作者的 ANES 代码中实施的 VOF(流体体积)模型和算法进行了交叉验证。计算使用 ANES 和 ANSYS Fluent CFD 代码进行。ANSYS Fluent 代码的预测结果证明取决于求解液体体积分数守恒方程的算法设置。为使预测结果与实验数据和理论关系更加一致,提出了设置该代码的建议。ANSYS Fluent 代码用于小型管束中制冷剂-21 冷凝的二维模拟。管束(库)的特征与俄罗斯科学院西伯利亚分院热物理研究所实验装置中使用的管束特征相同(管径 = 16 毫米,横向管束间距 \({{S}_{1}}\) = 26 毫米,纵向管束间距 \({{S}_{2}}\) = 15 毫米)。研究了饱和温度为 \({{T}_{{sat}}\) = 333.15 K、以最高 1.2 m/s 的速度到达管束的饱和蒸汽的凝结情况。预测结果表明与实验数据在定性和定量上一致。
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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