Thermal and viscous irreversibilities in the heat exchanger of individually finned heat pipes using freon R404A as the working fluid

Élcio Nogueira
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Abstract

This work aims to apply a theoretical procedure to determine the performance of the heat exchanger of individually finned heat pipes used in an air conditioning system. The relevant physical quantities are defined and specified locally in the evaporator and condenser sections. The results obtained in the sections are associated with the theoretical determination of the global performance of the heat exchanger. Global theoretical results are compared with global experimental results. Thermal effectiveness, heat transfer rate, pressure drop, thermal and viscous irreversibilities, and thermodynamic Bejan number are determined at the evaporator, condenser, and heat exchanger. The relevant variables used to determine the results are the number of fins per heat pipe and rows of heat pipes. The theoretical-experimental comparison demonstrates that the localized model applied in the analysis is consistent and can be used as a design and comprehensive analysis tool for finned heat exchangers. The performance of the heat exchanger demonstrated exceptional when comparing irreversibilities through the Bejan number, indicating a favorable cost-benefit ratio for the fins less than 30 and the number of heat pipes equal to 49. Bejan’s thermodynamic number, which uses results related to thermal and viscous irreversibilities, demonstrated that one should look for the relationship between thermal irreversibility versus total irreversibility and that fin numbers between 10 and 20 for heat pipes equal to 49 provide a better cost-benefit ratio. The absolute percentage errors obtained between theoretical and experimental values, for an experimental number of fins equal to 30, for the overall heat transfer rate and overall thermal effectiveness range from 2.0% to 42.1%.
使用氟利昂 R404A 作为工作流体的独立翅片热管热交换器中的热不可逆性和粘不可逆性
这项工作旨在应用一种理论程序来确定空调系统中使用的独立翅片热管热交换器的性能。相关物理量在蒸发器和冷凝器部分进行了局部定义和指定。各部分获得的结果与热交换器整体性能的理论确定相关联。全局理论结果与全局实验结果进行了比较。确定了蒸发器、冷凝器和热交换器的热效率、传热速率、压降、热不可逆性和粘性不可逆性以及热力学贝扬数。用于确定结果的相关变量是每根热管的翅片数量和热管排数。理论与实验比较表明,分析中应用的局部模型是一致的,可用作翅片式热交换器的设计和综合分析工具。在通过贝扬数比较不可逆性时,热交换器的性能表现出众,表明翅片数量少于 30 片、热管数量等于 49 根时,具有良好的成本效益比。贝扬热力学数使用了与热不可逆性和粘性不可逆性相关的结果,表明人们应关注热不可逆性与总不可逆性之间的关系,热管数量等于 49 时,翅片数量在 10 至 20 之间可提供更好的成本效益比。在翅片数量等于 30 的实验条件下,总传热率和总热效率的理论值与实验值之间的绝对百分比误差为 2.0% 至 42.1%。
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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