MODELS FOR HEAT TRANSFER CALCULATION DURING FILM CONDENSATION INSIDE HORIZONTAL TUBES

V. Gorin, L. Kolomiets, V. V. Sereda
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Abstract

The study of heat transfer during condensation in the middle of the pipes is relevant due to the constant need to improve the design of various heat exchangers (condensers of refrigeration and air conditioning systems, reactor safety systems, and power plant heaters). It is important to know the exact values of heat transfer coefficients in the case of condensation when their value is close to the heat transfer from the cooling side. Well-known theoretical, semi-empirical and experimental models and correlations for heat transfer calculation during condensation of working fluids inside smooth horizontal pipes have been described in the article. Selected models are widely used in various scien-tific publications for heat transfer prediction and construction of various heat exchangers with in-tube condensation. All correlations allow determining the average by tube perimeter, but local by the length of the tube, heat transfer coefficients in the case of annular and intermediate regimes of two-phase flow. All used dependences take into account current modes of phase flow. For choosing the best correlations, a comparison between selected models and experimental values of heat transfer coefficients obtained by different authors for condensation of ten working fluids inside smooth hori-zontal tubes with internal diameters more than 3 mm have been performed. Experimental values were selected from well-known works, in which heat transfer was studied during condensation of such fluids as fluorocarbons, immersion refrigerants, hydrocarbons and steam in the case of intermediate and annular phase flows with a detailed description of research conditions (geometrical parameters of investigated tubes and regimes parameters of condensation process, such as heat flux, mass velocity, vapour quality, and condensation temperature). Comparison of various models with experimental data of different authors allowed identifying the models that show the best convergence with experi-ments among all correlations. Recommendations (range of application) for use of models in engineer-ing practice are given.
水平管内膜状冷凝传热计算模型
由于不断需要改进各种热交换器(制冷和空调系统的冷凝器、反应堆安全系统和发电厂加热器)的设计,因此对管道中间冷凝过程中的传热进行研究是相关的。在冷凝情况下,当传热系数的值接近冷却侧的传热时,知道传热系数的确切值是很重要的。本文介绍了光滑水平管内工质冷凝传热计算的著名理论模型、半经验模型和实验模型及关系式。所选择的模型在各种科学出版物中被广泛用于各种管内冷凝换热器的传热预测和施工。所有的相关性允许确定平均管的周长,但局部管的长度,换热系数在环空和中间状态的两相流的情况下。所有使用的依赖项都考虑了相流的电流模式。为了选择最佳关联,将所选模型与不同作者获得的十种工质在内径大于3mm的光滑水平管内冷凝传热系数的实验值进行了比较。实验值选自知名著作,研究了氟碳化合物、浸入式制冷剂、碳氢化合物和蒸汽等流体在中间相流和环空相流下的冷凝传热,并详细描述了研究条件(被研究管的几何参数和冷凝过程的参数,如热流、质量速度、蒸气质量和冷凝温度)。将不同作者的各种模型与实验数据进行比较,可以确定在所有相关性中与实验表现出最佳收敛的模型。给出了在工程实践中使用模型的建议(应用范围)。
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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